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PROJECT AT A GLANCE Annual Production Capacity

Urea : 5,11,500 MT

Daily Capacity

Ammonia : 900 MT

Urea : 1550 MT

Plant On Stream Days : 330

Project Time Schedule : 36 months

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MILES STONE

1 ZERO DATE 29-01-2010

2 MECH.COMPLETION

28-10-2012

3 HOOKING UP 28-12-2012

4 COMMISSIONING 28-01-2013

5 ACCEPTANCE 28-03-2013

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Annual requirement of Raw

Material & Utilities

Natural Gas (LHV=8685 kcal/ Sm3)248 million Sm3

Support Natural Gas : 25.07 millionSm3

Coal (LHV=4150 kcal/ kg) : 320712 MT

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CAPITAL EXPENDITURE

Project Capital Cost

Total : Rs. 1294.19 Crore

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REIMBURSEMENT OF

CAPITAL EXPENDITURE(i) 80% of the Project Capital Cost,

disbursement in 5 Years, interest accrued on

it & income tax liabilities on above due torevenue generation in the form of SpecialFixed Cost.

(ii) Pre-set Energy norms allowed under NPS-IIIto be given post revamp for 5 (five) years formeeting balance Project Capital

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ENERGY/ MT AMMONIA(ISBL

UNIT Sp.cons.Heat value

(Gcal/unitEnergy

(Gcal/MT

NG KNM3 0.81 8.6857.078

100k steamimport MT 3.920 0.800 3.136power MWH 0.23 2.860 0.67040k steamexport MT -2.13 0.761 -1.621BFW export MT -0.87 -0.871total 8.392

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Ammonia

Plant

OilHandling/Storage

3 Aux Boilers1 Power Boiler

BaggingPlant

IA Dryers

UreaPlant

LPGStorage

MethanolStorage

CoalHandlingplant

TurboGenerator

DM Plant SulfurRecovery

CoolingTower

CO2 /dry ice

Treated water for irrigationE.T.P

Effluent from plants

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Ammonia

Plant

OilHandling/Storage

3 Aux Boilers1 Power Boiler

BaggingPlant

IA Dryers

UreaPlant

LPGStorage

MethanolStorage

CoalHandlingplant

TurboGenerator

DM Plant SulfurRecovery

CoolingTower

CO2 /dry ice

Treated water for irrigationE.T.P

Effluent from plants

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Air Separation Unit

Gasification section

Rectisol Section

SGP & CPP Section

De aerator, BFW Pumps& Steam section

N2 Compressor

Air Compressor

N.W.U

Synthesis Compressor

Synthesis Section

O2Compressor

Steam to Process& Turbines Ref.Compressor

NH3to Urea/storage

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Air Separation Unit

Gasification section

Rectisol Section

SGP & CPP Section

De aerator, BFW Pumps& Steam section

N2 Compressor

Air Compressor

N.W.U

Synthesis Compressor

Synthesis Section

O2Compressor

Steam to Process& Turbines Ref.Compressor

NH3to Urea/storage

New Ammonia Plant

CO2to Urea

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REDUNDANT SECTIONS OF THE PLANT Rectisol and ARU. CO-Shift Conversion. ASU and Nitrogen Wash Unit. Air, Oxygen and Nitrogen compressors. Gasification and Carbon Recovery. 64-ata steam network. Sulfur Recovery Plant.

Fuel Oil Storage and related facilities. CO2 supply to outside (dry Ice) plants shall be

stopped. S-200 Reactor. 3-ata steam net work shall reduce greatly. 3-ata

steam is required only in De-aerator.

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SECTIONS ON REDUCED LOAD Two Boilers shall be required to run instead

of present three Boilers.

Coal Handling and Ash Handling shall reducedby about 45%.

Cooling Tower (CT-1) load shall reduce frompresent 18000 M3/Hr. to about 12000 M3/Hr.

of CW flow. PW and BFW flows shall reduce by about

30%.

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