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OBJECTIVE
To render best services to the organization to be a part of the success

FUNCTIONAL SUMMARY
As an Operator in methanol project plant, role and responsibilities are
Methanol plant erection& commissioning
* Having 5 years of experience in Urea production plant.
* Worked in Windsor Satyam Engg., Company as a Operator for 1.5 Years
* Worked in BHEL for 1 year as a trainee.
* To monitor and operate plant parameters from field.
* To follow daily schedule jobs and to inform the deviations to shift in charge.
* To check for safety of the working system and of the personnel.
* To follow safe operating procedures.
* To train and instruct subordinates.

EMPLOYMENT
* Dec 2007 _ till date
Employer Name: Chemanol chemicals
KSA
Designation: Operator
ƒÞ
July2004 - Oct 2007
Employer Name: Nagarjuna fertilizers and Chemicals Limited
Kakinada, Andhra Pradesh
Designation: Operator
Operating Plant parameters from field
* Mar, 2002 - Feb, 2004
Employer Name: Madras Fertilizers Limited.
Designation: Operator
Operating Plant parameters from field

ƒÞ Sep1998 - March 2000
Employer Name:Windsor Satyam Engg., Company.
Designation: Operator
Operating Plant parameters from field

EDUCATION
SUMMARY OF QUALIFICATIONS

Year Qualification Class
1994-1995 10th class 1st
1995-1998 Diploma in chem. Tech. 1st
REFERENCES
S.Murali Mohan,
Manager,
UREA-1, NFCL.
Phnoe: 0884-2342035

VOLUNTEER EXPERIENCE
* Active participation in safety committee as rescue squad member.
* FIRST AIDER - St. John Amulance
* Participated in various work groups like TPM and 5S.
PLANT KNOWLEDGE

M/s Nagarjuna Fertilizers And Chemicals Limited is the biggest urea production unit in South India, accounts 8% of total production in the country and is the flagship company of Nagarjuna Group, which is involved in several major businesses. The Technical know-how is from SNAMPROGETTI, Italy for Urea plant and HALDOR TOPSOE, Denmark for ammonia plant. It is having two units, each of designed capacity 1750 MTPD of urea and 1200 MTPD of ammonia. It is having captive power generation units of capacity 33MW.

DCS: The distributed control system of plant is recently revamped with new Advant Controller 460 by ABB. The Advant Controller 460 (AC460) is suited for medium to large process control applications that require high performance and redundancy. CPU redundancy is available on 1:1 basis as an option Redundancy for DCN communication is Included in the basic unit with configurable options for power, and I/O redundancy. In Urea Plant, we have the following units, about which I have good knowledge over their operation:

STEAM TURBINE: A steam turbine of 9.57MW power drive CO2 compressor. It is partial condensing and partial extraction type turbine with hydraulic governor
(wood ward PG-PL)

CO2 COMPRESSOR:
A centrifugal compressor of 4 stages with a rated capacity of 40,000 NM3 /hr, supplied by M/S BHEL, driven by 9 MW steam turbine of partial condensation and partial extraction and LP steam injection Compressor is being operated under 0.56ksc suction pr. and 160 ksc final discharge pressure also incorporated with DRY GAS SEALS,supplied by M/S John Crane, U.K

PUMPS: High pressure 5 plunger reciprocating Ammonia feed pumps To Urea reactor, of PERONI make, Italy. It is being operated Under 20 ksc suction/240 ksc discharge and High pressure two stage centrifugal Carbamate pumps, Operated under 18 ksc suction/ 180 ksc discharge. In addition to the above, we are having number of Reciprocating and centrifugal pumps driven by LT motors.

REACTOR: A multi layered high pressure Urea reactor operating under 156 ksc,which had been revamped with 14 CASALE high efficiency trays in place of 10 Sieve trays in 1996 by M/SCasale,Italy
STRIPPER: A reversible CO2 Stripper with Titanium tubes, operating under 146 ksc, supplied by M/S FBM Hudson, Italy, which had undergone modification from internal ferrules to external Ferrules by using Zirconium sleeves.
HP, MP AND LP: The Urea purification is carried out through High pressure, Medium Pressure and Low pressure sections at146/18/3.5 respectively. In these section, it has pre heaters, Condensers, CO2 absorber, Ammonia Receiver, Ammonia Scrubbers for ammonia recovery, and Carbamate Condenser to generate LP steam (Around 60 Te), etc.

VACUUM SECTIONS: To concentrate Urea melt from 87.5% to 99.8%, it has two vacuum Concentrators (operating Under 0.3/0.035 ksc abs) preceded by one Pre Vacuum concentrator at 0.3 ksc abs.
WASTE WATER TREATMENT: In this section one Distillation Column, Hydrolyser, Pre heaters for heat recovery, etc., which treats around 50 m3 /hr of process effluent generated, to permissible limits for reuse in Demineralization Plant.

LANGUAGES KNOWN
Able to read and write English, Tamil
Able to speak Telugu, Hindi
DATE OF BIRTH
9 June 1980
NATIONALITY
Indian
MARITAL STATUS
Married

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