CURRICULUM VITAE

FROM M.V.SWAMY

D-No:*-**/*

GORSA

U.KOTHAPALLI MANDAL

EASTGODAVARI

ANDHRA PRADESH ,INDIA

PIN:533450

Phone no : +919*********

Email-Id : hjulys@r.postjobfree.com,

: hjulys@r.postjobfree.com

OBJECTIVE CAREER:

To associate myself with an organization offering a profession, challenging and rewarding work environment and gives me a chance to update my knowledge and enhance my skills and be a part of the team that excel in works towards the growth of the organization.

EDUCATIONAL QUALIFICATIONS:

Sl

No

Qualification

University/Board

Institution

Year of passing

%of

marks

1.

2.

.3..

BACHELOR OF SCIENCE IN PETROCHEMICAL

INTERMEDIATE

S.S.C

ANDHRA UNIVERSITY

P.R.Govt COLLEGE

KAKINADA

BOARD OF INTERMEDIATE EDUCATION

BOARD OF SECONDARY EDUCATION

Z.P.H. SCHOOL,

KOMARAGIRI

2005-2008

2003-2005

2002-2003

78.0%

87.10%

83.25%

PROFESSIONAL EXPERIENCE:

Organization : Nagarjuna Fertilizers and Chemicals Limited-Kakinada

Designation : OPERATOR (Production)

Duration : June 2008 – Till date

Plant profile : A HALDOR TOPSOE, DENMARK designed Ammonia plant

having a capacity of 1050 MTPD using Natural gas and Naphtha as a feedstock

ROLES AND RESPONSIBILITIES:

Controlling plant upsets and maintaining clear communication and coordination with other sections of the plant.

Operating, monitoring and controlling assigned work area through DCS stations safely & efficiently.

Condition monitoring of all rotary equipments, reporting all equipment, instrument defects and leads immediately to shift In Charge and taking possible corrective actions.

Periodical logging of parameters, regular routine checks of all equipments and units to ensure that they are functioning correctly in accordance with standard operating procedures.

Providing reliable and accurate information on plant condition and status to the Shift Supervisor and Shift Controller regarding maintenance activities and daily management reports.

Handling emergency incidents (Fire, Gas leak, Plant Shutdowns etc.) and ensure emergency plans and procedures are adhered to.

WORK EXPERIENCE:

Experience in various process such as Hydrodesulphurization, Reforming, Shift Conversion,Co2 absorption and removal,Methanation,Compression, Synthesis of Ammonia and Purge gas Recovery unit

Experience in handling various equipments like turbines of different types, multistage centrifugal pumps, High Pressure Compressors, Boilers and Duplex side fired Reforming furnace and catalytic vessels

Experience in unit operations such as absorption, adsorption etc

Familiar with Emergency Shutdown systems and PLC based Equipments

Experience in cooling tower operations.

WORK PROFILE:

Worked in ammonia production plant .Controlling , monitoring and recording the process parameters of all the sections concerned with outmost priority to safety .Taking part in daily activities like field rounds, vibration monitoring, bearing temperature monitoring physically, handling of fire and safety equipments depending on necessity, good housekeeping practices.

Reforming inspection for any flame impingement, doghouse hotspots, shell bulging, shell hot spots, tube hotspots-hot bands, refractory damage, measuring skin temperatures with Laser beam pyrometer

Special EXPERIENCE:

1). Catalyst loading, unloading of primary reformer.

2). Secondary reformer catalyst scooping, De-Sulph beds.

3). Good exposure to various problems such as in primary reformer

4). Hot bands due to aging of catalyst

5). Tube reducers failure due to carbonization of tube

6). Milling of catalyst after catalyst loading

7). Problems related to centrifugal ,Reciprocating compressors , centrifugal pumps.

INDUSTRIAL EXPERIENCE

Presently working as operator in M/s. Nagarjuna Fertilizers & Chemicals Limited, Kakinada from June 2008.NFCL an ISO-9001-2000 series, ISO-14000 & ISO-18000 certified company & also was honored a 5 star honor from British safety council, is having a design capacity of 1800MT per day of Ammonia 3000MT per day of Urea from 2 plants. I have been in 3 annual turnarounds of the plant and having good hands on experience in startups, shutdowns and trouble shootings of ammonia plant. I have experience in operation of compressors, high-pressure pumps, Low-pressure pumps single as well as multistage and vacuum systems . I have good knowledge and working experience in all sections of Plant, it covers all gas, liquid handling.

PLANT PROFILE:

M/S Nagarjuna Fertilizers and Chemicals Ltd. Is one of the largest largest Urea manufacturing fertilizer plants of India and biggest in south India and first to be based on natural gas. It is a Rs. 2,500 crore project, located at Kakinada; A.P. NFCL successfully completed its expansion project of similar capacity (each of 1050 MTPD of ammonia) and now running efficiently with mean 130% over the calendar year.

Ammonia process technology is supplied by M/S Haldor Topsoe of Denmark and designed by Snamprogetti, Italy. NFCL is having its own boilers, utilities and captive power generation (33MW). M/S NFCL conferred with ISO-9002 and ISO-14001 Certification from BVQI. Recently has gone for OHSAS-18001 and achieved a 5STAR honor from British Safety Council.

I have good knowledge and experience in all sections of Ammonia plant. Plant consists of the following sections.

NAPTHA STORAGE: Floating roof atmospheric pressure tanks,

Raw Naphtha: 2 nos. – Capacity; 3450 KL

Sweet Naphtha: 1No – Capacity, 7050 KL

SULPHUR REMOVAL SECTION:

PRE DESULPHURIZATION: It Consists deaeration, hydrogenation and

Stripper Sulphur content in the Naphtha is

Reduced to a level of 10 ppm

FINAL DESULPHURIZATION: It Consists feed stockpreheater,hydrogenator

and H2S ABSORBERS. Sulphur content is

reduced to a level of 0.01 ppm

REFORMING SECTION: System consists of adiabatic pre-reformer,

Primary Reformer and Secondary Reformer.

Methane content is reduced to 0.2%

ADIABATIC REFORMER: Having Catalyst RKNGR contains magnesia

(Mgo) Operating at 550 o c. It reforms higher

hydrocarbons into Lower hydrocarbons.

PRIMARY REFORMER: Side firing reformer having 190 tubes in two

Chambers subjected by 360 Natural gas/

Naphtha Burners. The nickel based catalyst

operating at 35Ksc/ 730 o c.

SECONDARY REFORMER: Having Catalyst RKNGR contains magnesia

(Mgo) operating at 550 o c. It reforms higher

hydrocarbons into lower hydrocarbons.

CO-CONVERSION : High temperature, Iron-chromium catalyst

CO-Converter and Low temperature

Zinc-copper catalyst CO-converter

Operating at 350 o c and 190 o c.

ACID GAS REMOVAL

SECTION: Giammarco Vetrocoke (GV) solution

Absorption Process. Absorption columns

operating at 30Ksc.

By feeding lean and semi lean solutions,CO2

Slip outlet of absorber is reduced to 500

PPM.

Regeneration takes place in HP regenerator

steam input operating at 1.1 Ksc and in LP

regenerator by flashing and operating at 750

mm of water column, boosting up the CO2 to

0.8 Ksc by booster compressor.

SYN.GAS LOOP AND

CONVERTER: Syn.gas loop waste heat boiler, heat

exchanger,Chillers, coolers and separators

operating at 149 Ksc iron based converter

having two beds with Inter cooling heat

exchanger and cold shot.

PRODUCT AMMONIA

AND WASH SECTION: The separated ammonia is purified in

letdownVessel at 25Ksc and flash vessel at

0.1 Ksc and Ammonia pumps. Ammonia

vapour from letdown vessel feed to

absorber and distillation column operating

at 15 Ksc and 20 Ksc respectively.

REFRIGERATION UNIT : The Syn.Gas in loop is cooled to - 13 c by

Operating Ammonia refrigeration chillers at

6ksc and 1.2 ksc.

CRYOGENIC SECTION: PROGRAMME LOGIC CONTROLLER

Based Cryogenic unit for hydrogen recovery

from loop Purge gas supplied by COSTAIN,

UK.

FURNACES: Natural draught and balanced draught

Furnaces.

BFW TREATMENT

AND BOILERS: Deaeration, Chemical dosing and high

pressure BFW pumps, two waste heat steam

boilers and Steam superheated operating at

105 Ksc

STEAM TURBINES: Extraction and condensing type turbine

(20MW, 108 KSC, 510 o C inlet flow 240

T/HR) to drive centrifugal synthesis gas

compressor supplied by Hitachi, Japan.

Injection cum condensing type steam turbine

(9MW, 39 ksc, 370 o C) drive centrifugal

process air compressor supplied by

MANGHH Germany.

Condensing type turbine (6.5MW, 39 ksc,

370 o C) to drive centrifugal ammonia

refrigeration supplied by MANGHH

Germany.

COMPRESSORS: We have both Centrifugal and Reciprocating

Type Compressors.

CENTRIFUGAL

COMPRESSORS: a) 4 stage horizontal split casing process air

Compressor which sucks ambient air and

Compress it upto 34 ksc with dry seals

(ambient air) Capacity : 55085nm3/hr.

b) 4 stage vertical split casing synthesis gas

Compressor in 3 stages. It compresses make-

up as from 24.5 ksc to 145 ksc. Fourth stage

is recirculator to increase synthesis gas

pressure from 140 to 150 ksc. With oil seals.

Make-up gas Capacity: 1,50,000 nm3/hr.

Recirculator Capacity: 6,00,000 nm3/hr.

c) 3 stage horizontal split casing Ammonia

Refrigeration Compressor is to compress

Ammonia vapors from 0.05 ksc to 25 ksc with

Oil seals.

RECIPROCATING TYPE

COMPRESSORS: Double acting horizontal balance opposite

Crosshead type reciprocating compressor for

Compressing Recycle gas supplied by

Khosla-Crepelle.

COOLING TOWERS: It consists of 2 pumps of capacity

18,000 NM3 /HR. Driven by 1.2 MW motor

and 1 pump driven by condensing type

turbine. Tower designed by Paharpur

Cooling Towers.

PERSONAL PROFILE:

Name : M.V.SWAMY

D.O.B : 01.06.1988

Father’s Name : M.N.SATYANARAYANA

Marital status : Unmarried

Permanent Address : D-No:1-60/1,GORSA,U.Kothapalli Mandal,E.G.Dt.

Languages Known : Telugu and English.

Mobile Number : +919*********

Hobbies : HEARING MUSIC, PLAYING CRICKET

INTROSPECTED ASSESSMENT:

Positive approach towards life makes for the ability to work under pressure as a competitive and tolerant team member.

DECLARATION:

I hereby declare that the above mentioned information is correct up to the best of my knowledge and I bear the responsibility for the genuineness of the particulars furnished above.

Place : KAKINADA Yours Truly,

Date : (M.V.SWAMY)

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