2. WELCOME

3. IFFCO AONLA UNIT, BAREILLY (U.P.)
WELCOME
HONOURABLE CPCB
OFFICIALS,ENGINEERS
& DELEGATES
AT
IIT-ROORKEE

4. ENVIRONMENTAL MANGEMENT
AT
IFFCO AONLA UNIT, BAREILLY (U.P.)

5. IFFCO - In Brief

6. IFFCO’S PLANTS
6

7. IFFCO PLANTS
KALOL UNIT PHULPUR UNIT
CORPORATE OFFICE
NEW DELHI
Year of Commissioning - 1975 Year of Commissioning - 1981
Annual Ammonia Capacity - 363000 MT Annual Ammonia Capacity - 824000 MT
Annual Urea Capacity - 544500 MT Annual Urea Capacity - 1415700 MT
KANDLA UNIT AONLA UNIT
PARADEEP UNIT
Year of Commissioning - 1975 Year of Commissioning - 1988
Annual P2O5 Capacity - 910000 MT Year of Acquire - SEP-2005 Annual Ammonia Capacity - 1003200 MT
Annual N Capacity - 351540 MT Annual Capacity -2000000
7 Annual Urea Capacity - 1729200 MT
MT

8. KALOL UNIT
GUJRAT
YEAR OF COMMISSIONING : 1975
INVESTMENT : Rs. 71.23 Cr.
YEAR OF EXPANSION : 1997
INVESTMENT : Rs. 149.70
Cr.
PRODUCT CAPACITY
TPD TPA
AMMONIA 1100 3,63,000
UREA 1650 5,44,500
„N‟ 759 2,50,470
8

9. KANDLA UNIT
GUJRAT
YEAR OF COMMISSIONING : 1975
INVESTMENT : Rs. 24.26 Cr.
YEAR OF FIRST EXPANSION : 1981
INVESTMENT : Rs. 28.60 Cr.
YEAR OF SECOND EXPANSION : 1999
INVESTMENT : Rs. 205.30 Cr.
PRODUCT CAPACITY
TPD TPA
„ P2O5 2890 9,10,100
„N‟ 1115 3,51,540
9

10. AONLA UNIT
UTTAR PRADESH
YEAR OF COMMISSIONING : 1988
INVESTMENT : Rs. 651.6 Cr. AONLA- I
YEAR OF EXPANSION : 1996
INVESTMENT : Rs. 954.7 Cr. AONLA- II
PRODUCT CAPACITY
TPD TPA
AMMONIA 3040 10,03,200
UREA 5240 17,29,200
„N‟ 2410 7,95,430
10

11. PHULPUR UNIT
UTTAR PRADESH
YEAR OF COMMISSIONING : 1981
INVESTMENT : Rs. 205.2 Cr.
Phulpur - 1
YEAR OF EXPANSION : 1997
INVESTMENT - Phulpur-II : Rs.1190 Cr.
PRODUCT CAPACITY
TPD TPA
AMMONIA 2497 8,24,000
UREA 4290 14,15,700
„N‟ 1973 6,51,222
11

12. PARADEEP UNIT
ORISSA
COST OF ACQUISITION Rs. 2589.88 Crore
(September 2005)
PRODUCT CAPACITY
TPD TPA
PHOS. ACID 2650 8,75,000
SULPHURIC ACID 6970 23,00,000
P2O5 2650 8,75,000
N 1006 3,32,000
12

13. IFFCO - AN ORGANISATION
FOR THE FARMERS
OF THE FARMERS
BY THE FARMERS

14. Origin of IFFCO
 IFFCO was established on 3rd
Nov.,67 as a co-operative of
farmers to produce & market
fertilisers.

15. IFFCO – In Brief
 Leading producer of fertilisers in India
 No. of plant locations - Five
 Installed Annual Capacity
Urea : 3.69 Million Tonne
NPK/DAP : 4.42 Million tonne

16. IFFCO – In Brief
 Contributes 18.3% to the total”N” and
50% to the total “P2O5” produced in
the country.
 Fertiliser marketed through around
37,500 cooperative societies and 158
Farmers Service Centres
 Service to the farmers through a
variety of programmes

17. Vision & Mission
Honorable Managing Director
Shri U.S.Awasthi
Under the dynamic leadership of our
Honorable Managing Director
Shri U. S. Awasthi IFFCO has drawn out
plans to grow manifold in fertiliser
sector as well as in allied areas.

18. Recently Implemented
Projects
AONLA EXPANSION PROJECT
PHULPUR EXPANSION PROJECT
KALOL EXPANSION PROJECT
KANDLA EXPANSION PROJECT
ACCUISITION OF OSWAL
FERTILISERS(Phosphatic)

19. Joint Ventures
JV FOR PHOS. ACID IN SENEGAL
DIVERSIFICATION IN INSURANCE
OMAN GRASSROOT PROJECT
IFFCO-AIR TEL FOR RURAL
COMMUNICATION

20. Vision-2010
Targets have been set to achieve group
turnover of Rs 15000 crore and annual
profit of Rs 1500 crore. Areas
contemplated for future growth include :
 Power  Phos. Acid
 Bio Fuels  Agri Business &
 Renewable Exports
Energy  Petroleum & Natural
 Banking Gas
 New Fertiliser  Petrochemicals
units  Telecommunications

21. Vision-2010 (contd…)
Investment plan for expansion in Fertiliser
sector and diversification into Power
sector at an estimated outlay of Rs 9000
crore :
 De-bottlenecking of existing plants for
Capacity enhancement.
 Mining project & Phosphoric acid plant at
Egypt and Jordan
 Acquisition of DAP & NPK facilities at
Paradeep in Orissa
 1000 MW Power project in State of
Chattisgarh

22. IFFCO
AONLA UNIT
ENERGY EFFICIENT
COST- CONSCIOUS
ECO-FRIENDLY & SAFETY CONSCIOUS
HARMONIOUS INDUSTRIAL ENV.
ISO-9001, ISO-14001 & OHSAS-18001
CERTIFIED

23. IFFCO Aonla Unit
…at a Glance

24. SONIPAT
SAHIBABAD
6” (20 KM)
HBJ Gas BAHADURGARH
6” (52 KM)
DESU
DADARI
24” (104 KM)
Pipeline 12” (35 KM)
MARUTI
18” (47 KM)
S‟
BAD
TCL 24” (82 KM)
MATHURA
Network 14” (13 KM)
24” (90 KM)
OCFL
24” (143 KM)
36” (505 KM)
NTPC 18” (217 KM)
12” (2 KM)
IGCL
AURAIYA CS Jagdishpur
12” (32 KM) (5 NOS COMPRESSORS)
CFCL
SAMCOR BORARI 30” (321 KM)
ANTA 18” (110 KM)
12” (14 KM)
NFL
18” (3.6 KM)
LPG
VIJAIPUR CS (8 NOS COMPRESSORS)
36” (340 KM)
18” (1.1 KM)
GSFC
LPG JHABUA CS (10 NOS COMPRESSORS)
Aonla Unit based on
IOC, IPCL 36” (150 KM)
18” (32 KM)
KAWAS VAGHODIA CS HBJ pipeline
12” (8 KM) 36” (149 KM)
DPD HAZIRA CS 1225 Km from Hazira
EX HAZIRA CONSUMERS - KRIBHCO, RPL, ESSAR, HWP, GGCL

25. Ammonia Plant-I Ammonia Plant-II
Production started on : 15.5.1988 Production started on : 13.12.1996
Capacity : 1520 MTPD Capacity : 1520 MTPD

26. Urea Plant-I Urea Plant-II
Production started on :18.5.1988 Production started on :26.11.1996
Capacity : 2620 MTPD Capacity : 2620 MTPD

27. Railway Siding
Product Handling Plant 9.38 KM Railway Siding on 110 Acres land
In-plant yard comprising of 12 lines
Capacity : 2x8 Bagging
Naphtha / Fuel oil 4 lines on RCC apron
Stations (Slat) @ 60 MTPH
Capacity - Silo - I & II
Silo-I : 45000 MT
Silo-II : 30000 MT

28. Power Plant
Capacity :
Steam generation
plant : 150 MT/Hr
Power generation
Plant :
GTG : 2X18 MW/Hr
HRSG : 2X80 MT/Hr

29. Cooling Towers
Number of cells -
 Urea Plant : 5 nos. each for Urea- I & II
 Ammonia Plant :6 nos. each for Ammonia-I & II

30. Ammonia Storage Tanks
Capacity : 2x10,000 MT

31. Lagoons
Capacity : 2 x 85000 M3

32. Birds in Lagoon

33. Fire & Safety

34. IFFCO Aonla Unit
 IFFCO Aonla Unit was set up at Aonla,
Bareilly in the year 1988 to increase the
fertiliser production in the country under
the overall national planning for utilisation
of natural gas available from Bombay
High.
 In the year 1996 the production capacity
was doubled with the commissioning of
Aonla-II.

35. Main Plants & Auxilliary Facilities
Aonla-I Aonla-II
Ammonia Plant 1520 MTPD 1520 MTPD
(1740 MTPD) (1740 MTPD)
Urea Plant 2620 MTPD 2620 MTPD
(3030 MTPD) (3030 MTPD)
S.G. facilities (116 Kg/Cm2, 515 Deg C)
• Service Boiler 150 MTPH
• Heat Recovery Unit 80 MTPH (80+120) MTPH
Gas Turbine 25 MW 25 MW
Generator (ISO)

36. Main Plants & Auxilliary Facilities
(Contd…)
Instrument / Plant 6 X 1200 NM3/Hr
Air Compressor 1X5000 NM3/Hr
Water Treatment Plant 6 x 140 M3/HR
Inert Gas (N2) Generation 600 NM3 /HR
Ammonia Storage Tank 2 x 10,000 MT
Air & Steam Stripping Unit Of (60+45) M3/Hr
Ammonia Bearing Waste

37. Main Plants & Auxilliary Facilities
(Contd…)
UREA BAGGING PLANT 2X8 Bagging
Stations
@ 250 MTPH
FUEL OIL / NAPHTHA STORAGE
Fuel Oil Storage 2 x 3650 M3
Naphtha Storage 2 x 6000 M3
1 x 10000 M3
UREA SILO Aonla-I 45000 MT
Aonla-II 30000 MT

38. IFFCO-AONLA UNIT GOT SEVERAL AWARDS AND CERTIFICATES FROM VARIOUS
AGENCIES ,FOUNDATIONS, GOVERNMENT BODIES AND INSTITUTES
SHE RELATED AWARDS RECENTLY WON BY IFFCO AONLA UNIT
CII AWARD FOR ENERGY FOR EXCELLENCE IN ENERGY MANAGEMENT 21&22,AUG,2006
“RUNNER UP” IN NATIONAL SAFETY AWARDS-2times Ministry of labour & employment ,
Govt. of India 07-09-2005,sept2007
NSCI AWARDS-2004&2006 “PRASHANSHA PATRA” National Safety AWARD RECEIVED IN
Council of India APRIL,2006&jan 2007
“GOLDEN PEACOCK” SPECIAL COMMENDATION OF
World environment Foundation 11-06-2005
ENVIRONMENT MANAGEMENT AWARD-2005
“CERTIFICATE OF PARTICIPATION” CORPORATE TERI Corporate Environmental Awards
ENVIRONMENTAL AWARDS-2002/03 05-06-2004
NSCI AWARDS 2000 &-2002 “PRASANSHA PATRA” National Safety
27-12-2003,10-12-2002
Council of India
“CERTIFICATE OF MERIT” NATIONAL ENERGY National Energy Conservation in
Fertiliser Sector by Ministry of Power,
CONSERVATION AWARD-2003 Govt. of India 14-12-2003
“CERTIFICATE OF MERIT” NATIONAL ENERGY National Energy Conservation in
Fertiliser Sector by Ministry of Power,
CONSERVATION AWARD-2002 Govt. of India 14-12-2002
FAI AWARD FOR EXCELLENCE IN SAFETY2001-02,2005-06 FAI, ,05-12-2007 & 16-12-2002
38
NATIONAL ENERGY CONSERVATION AWARD-2006 (2Nd) 14TH DEC,2006, BY MIN OF POWER

39. Awards

40. Awards (Contd…)
THE FERTILISER ASSOCIATION OF INDIA‟s AWARD FOR
EXCELLENCE IN SAFETY

41. Awards (Contd…)
NATIONAL ENERGY CONSERVATION AWARD, 2002 FROM
MINISTRY OF POWER

42. Awards (contd…)
NATIONAL SAFETY COUNCIL OF INDIA
SAFETY AWARDS-2000

43. Awards (Contd…)
THE FERTILISER ASSOCIATION OF INDIA‟s AWARD FOR
BEST ARTICLE

44. Awards (contd…)
IFFCO-Aonla unit has bagged National Energy
Conservation Award-2003 : Certificate of merit

45. Awards (contd…)
IFFCO-Aonla unit has won the NSCI Safety Award
(Prashansa Patra) for the year 2002

46. Awards
GOLDEN PEACOCK ENVIRONMENT MANAGEMENT
AWARD-2005 (CERTIFICATE OF COMMENDATION)

47. Awards(Contd)
NATIONAL SAFETY AWARD -2004 (RUNNER UP UNDER SCHEME-II)
Award was presented by Sh K M Sahani, Hon‟ble Secretary,
Ministry of Labour & Employment for outstanding
performance in industrial safety during the year 2004
based on longest accident free year

48. Awards (contd…)
RAJIV RATNA NATIONAL AWARD-2005 : BEST EXECUTIVE
GOLD AWARD FOR SH H C DAVE, EXECUTIVE DIRECTOR

49. Awards (contd…)
PRASHANSHA PATRA
FOR THE YEAR 2004&06 FROM
NATIONAL SAFETY COUNCIL
FOR DEVELOPING AND
IMPLEMENTING OCCUPATIONAL
SAFETY & HEALTH MANAGEMENT
SYSTEMS & PROCEDURES

50. NSCI AWARD-2004

51. Awards (contd…)
ICQESMS-2005 &2007 EXCELLENCE
AWARD
FOR PAPER PRESENTED IN
4TH INDIAN CONGRESS ON
QUALITY, ENVIRONMENT, ENERGY AND
SAFETY MANAGEMENT SYSTEM-BY
CBWE & JADHAVPUR UNIVERSITY

53. ENERGY AWARD

54. CII AWARD

55. NSA AWARD-2006

56. FAI AWARD –SAFETY 2007

58. Production
Performance
- A Brief Overview

59. Production Performance
UREA PLANT-I
Annual Capacity v/s Actual Production (Lakh MT)
8.65 8.65 8.65 8.65 8.65 8.65 8.65 8.65 8.65
8.7
8.6
8.5
Production ( lakh MT )
8.4
8.3
8.2 8.14
8.1
8
7.9
7.8 2000-01 2003-04 2004-05 2005-06 2006-07
Capacity Actual Production

60. Production Performance(Contd.)
UREA PLANT-II
Annual Capacity v/s Actual Production (Lakh MT)
8.65 8.65 8.65
8.64 8.65 8.65 8.65
8.65 8.65
8.58
9
8
7
Production ( lakh MT )
6
5
4
3
2
1
0
2000-01 2001-02 2002-03 2003-04 2004-05
Capacity Actual Production

61. Energy
Conservation -
A major concern

62. Reduction In Overall Specific Energy
Consumption (Aonla-I+II)
OVERALL ENERGY OF THE COMPLEX
(GCAL/TE UREA)
1998-1999 1999-2000 2000-2001 2001-2002 2002-2003 2003-2004 2004-2005 2005-2006
5.9303 0.0646
0.1305 0.2598
0.3060 0.2901
0.2893 0.3570
5.8657
5.7998
5.6705
5.6243 5.6402 5.6410
5.5733

63. Environment Management

64. Environment Management
Awards & Certifications
 Bagged Indo-German Greentech Environmental
Excellence Award for 2 consecutive years (in 1999-
2000 and 2000-2001).
 Bagged Corporate Environment Award 2002-03
(certification of participation) from TERI in recognition
of the efforts made towards Environment
Management and sustainable initiatives.
 Bagged Golden Peacock Environment Management
Award-2005 (Certificate of Commendation).
 Achieved ISO 14001 certification for Plant and
Township.
 Achieved OHSAS-18001 certification.

65. Green Belt Development
 The project site was completely barren with
high soil alkalinity.
 Developed 80-M WIDE GREEN BELT around plant
and township.
 Aforestation with about 1,70,000 TREE
PLANTATION.
 Soil Treatment by using pyrite alongwith
Gypsum, sweet soil topping up and cow-dung.

66. Environment Management
Approach
 Technology Selection on Zero - effluent concept
based on Recycle and Reuse of Waste Water.
 Maximum reuse of treated water in the irrigation
of green belt and lawns in the plant and township.
 Developed 80 to 250 meter wide green belt in &
around the plant and township.
 Education and training of employees and
awareness to residents of nearby areas regarding
environmental issues

67. Environment Management
Approach (contd…)
 Environmental laboratory with pH meter,
conductivity meter, SOx / NOx analyser, High
Volume Sampler and Spectrophotometer etc.
 Continuous monitoring of quality of Ground water,
Effluent, Stack emissions and Ambient Air.
 Environmental Management Cell for day to day
monitoring , control , Environmental Auditing,
Setting goals i.e Objectives & Targets for reduction
of wastages in all forms.

68. Pollution Abatement Facilities
Ammonia Plants
 Process Condensate
Contaminated Process Condensate
undergoes stripping process in
CONDENSATE STRIPPER with the help of
steam . In this process impurities like CO2 ,
NH3 and CH3OH are stripped off. It is then
treated in Polishing Unit and recycled as
Boiler Feed Water.

69. Pollution Abatement Facilities (Contd…)
Ammonia Plants (Contd…)
 Purge Gas Recovery Unit to recover Hydrogen
from Purge gas.
 Total Recycle of Turbine Condensate.
 Reuse of Boiler Blow Down For cooling Tower
Make-Up.
 Separation and Collection of Oil from Oily Water
by means of Disc Oil Separator.
 Separation & Collection Of Occasional
Ammonical effluents for treatment in ETP.

70. Pollution Abatement Facilities
Urea Plants
 Segregation,collection & Total Recycle of urea
bearing waste after processing in Deep
Hydrolyser and using the treated effluent as BFW
make up after polishing. Ammonia & CO2 are
recycled back to the process.
 Collection of occasional spill for treatment at
Centralised Effluent Treatment Plant.
 Separation and collection of oil From oily water
by means of Disc Oil Separator.
 Urea Prilling Towers (96 m & 104 m)

71. Pollution Abatement Facilities (Contd…)
D M / Water Treatment Plant
 Polishing Unit for the treatment of
process/steam/ turbine condensates from
the plants.
 Segregation, Collection & Neutralisation of
Acidic and Alkaline Effluents.
 Utilisation of Acidic & Alkaline effluent for
pH control.
 Absorption of Acid vapor fumes by water
spraying.

72. Pollution Abatement Facilities (Contd…)
Product Handling plant
 Dust collection and it‟s
reprocessing
 Collection of swept urea and
it‟s reprocessing

73. Pollution Abatement Facilities (Contd…)
Centralised Effluent Treatment Plant
 Treats ammonia bearing occasional waste water from urea
and ammonia plants with Air/Steam Strippers.
 Stores treated effluent in LDPE lined lagoons for green belt
irrigation and functions as a buffer. These lagoons attract
large number of migratory birds in winter months.
 Plant is having facilities for removal of Vanadium
(occasional discharge) from GV system by precipitation
and storage in secured lined pit.

74. EFFLUENT FLOW SCHEMATIC DIAGRAM
ACIDIC AND ALKALINE EFFLUENT
ACID AND ALKALY
OILY OILY DISC OIL NEUTRALI- DOSING FOR PH
EFFLUENT SEPARATOR SATION PIT CORRECTION
WATER
OVER FLOW TREES
LIME
AMMONICAL
EFFLUENT TO ARIL
HOLDING AIR & STEAM HOLDING
RIVER
STRIPPERS
PIT GUARD
PIT
AND V2O5 PONDS
OCCASIONAL
REMOVAL
EFFLUENT 2X85000
FROM UREA M3
TREES
C.T
BLOWDOWN
FOR
IRRIGATION
OF GREEN
BELT
ACIDIC
ALKALINE ACIDIC NEUTRALISATION
EFFLUENT
ALKALINE PIT

75. Pollution Abatement Facilities (Contd…)
On Line Monitoring of Stack Emissions & Liquid
Effluents
 Online SO2, NO2, O2 Analysers in Ammonia and
Power Plants.
 On line pH meters, conductivity meters and silica
analysers in DM Plant, Ammonia , Urea and Power
Plants.
 On line pH meter and Ammonia analyser on factory
discharge.
 Ammonia analysers in Ammonia storage area.

76. Pollution Abatement Facilities (Contd…)
Township
 ISO 14001 certified township.
 Irrigation of green belt and lawns by treated
effluent , thus saving natural resources like
water.
 Safe collection and disposal of township as
well as Plant canteen solid waste.
 Conversion of township/plant solid garbage
into Vermi-compost

77. Pollution Abatement Facilities (Contd…)
Environment & Pollution Control Cell
 Obtaining and renewal of Water/ Air Consent every
year and implemented it‟s conditions continuously.
 Obtaining and renewal of Hazardous waste/Bio-
medical Wastes Authorisation and implemented
it‟sconditions.
 Implemented CREP recommendation.
 Safe Storage & disposal of Hazardous Wastes (spent
catalyst and spent oil) as per CPCB guidelines.
 Submission of Annual Environmental statement.

78. CO2 Recovery From Flue Gas:
• In Aonla Unit, Lean NG is being supplied by
GAIL through HBJ pipeline which results in CO2
shortage for conversion of full Ammonia
production to Urea leading to Ammonia stock
buildup in the plant.
• CO2 recovery has been installed to meet the
shortfall of CO2.
• CO2 recovery Plant is recovering 450 MTPD of
CO2 from the Primary Reformer flue gases of
Ammonia-I (A CDM Project).

79. CO2 to Urea plant
Flue gases to (CO2 : 99%min. dry
atmosphere basis)
Flue gases
CO2
to
Blower
atmosphere
Flue gas
Blower Lean solution
Absorption Regeneration
ID Fan Rich solution
LP Steam
Flue gases from Primary CDR Unit
Reformer (CO2 : 10-
12%dry basis)

80. Water Consumption (m3/hr)
Consumption Pattern 2005-06 2006-07
Plant 240 250
Cooling Tower 940 830
Domestic&Miscellaneous 160 130
Total water consumption 1340 1210

81. Water Consumption (yearly)
Consumption Pattern 2005-06) 2006-07
Total water consumption 10660053 9551476
Urea Production 1737580 1770103
Water Consumption/MT of 6.135 5.396
Urea

82. Liquid Effluent Generation
Plant Qty. (m3/hour)
Ammonia (Occasional 6
waste)
Urea(Occasional waste) 12
Cooling Tower 180
DM Plant 40
Total 238
For Irrigation Purposes 128
Discharge to Aril River 110

83. Details of Primary Reformer Stack of both
Ammonia Plants
Sr.No Descripn.
Amm-1 Amm-2
1 Installed 1520 1520
Capacity
MTPD
2 Type of NG NG
Fuel
3 Height of 30 30
Stack(M)
4 Flue gas 2,25,000 1,90,000
flow rate
NM 3 /hr.

84. Details of Primary Reformer Stack of both
Ammonia Plants (contd…)
Sr.No Particulars
. Amm-1 Amm-2
5. Flue gas 160 139
Temp.0C
6. Eflux 9.4 7.9
Velocity,m/sec
.
7. SO2 Conc. Traces Traces
(ppm)
8. Nox Conc. <70 <70
(ppm)

85. Details of Prill Towers
Sr. Particulars
No. Urea-1 Urea-2
1. Installed 2600 2600
capacity
(MTPD)
2. Height of Prill 104 96
Tower
(m).
3. Air Flow 1.06X106 1.27X106
(nm3/hr.)
4. Exhaust air 53 50
Temp. (0C)
5. Ambient Air 22 22
Temp. at
Ground Level
(0C)

86. Effluent Analysis
(Factory Discharge)
Sr. Parameter Unit Standard Avg Avg Avg
No. Value Value Value
(2004-05) (2005-06) (2006-07)
1. pH ---- 6.5 – 8.0 7.40 7.52 7.7
2. Ammonical PPM 50 9.87 11.98 11.92
Nitrogen
3. Free- PPM 5 1.60 00.53 0.53
Ammonia
4. Total Kjeldahl PPM 100 33.70 18.27 24.99
Nitrogen

87. Pollutants unit Standard of Annual % Increase
UPPCB Average /Decrease
concentration (+)/(-) of
of Pollutants Pollutants
pH - 5.5-9.0 7.70 ---
Cr+6* mg/L 0.1 NT ---
Total Cr* mg/L 0.5 NT ---
Oil/ Grease mg/L 10 NT ---
Ammoniacal mg/L 100 11.92 (-)88
Nitrogen as N
T.K.N. mg/L 150 24.99 (-)83.6
T.S. S mg/L 100 33.33 (-)66.67
Free NH3 mg/L 5.0 0.53 (-)89.4
B.O.D mg/L 30.0 15.82 (-)42.6
C.O.D mg/L 250.0 39.24 (-)84.3
Phosphate as mg/L 5.0 0.65 (-)87
PO 4

88. ANALYSIS OF STACK EMISSIONS
(AMMONIA PLANTS)
Plant parameter Unit Standards Avg Avg Avg
Value Value Value
(2004-05) (2005-06) (2006-07)
Ammonia-I SPM Mg/Nm3 500 NT NT NT
SOX PPM 100 Traces Traces Traces
NOX PPM 100 74 72 70
Ammonia-II SPM Mg/Nm3 500 NT NT NT
SOX PPM 100 3.14 Traces Traces
NOX PPM 100 58 42 32
PPM

89. ANALYSIS OF STACK EMISSIONS
( PRILL TOWER UREA DUST EMISSION)
Plant Parameter Unit Standard Avg Avg Value Avg Value
Value (2005-06) (2006-07)
(2004-05)
Urea I
SPM Mg/nm3 50 26.90 40 38.59
Urea Dust
Ammonia PPM 50 30.48 30 30
Urea II SPM Mg/nm3 50 27.64 38 35.85
Urea Dust
Ammonia PPM 50 36.54 36 36

90. ANALYSIS OF STACK EMISSIONS
(STEAM & POWER GENERATION PLANT)
Plant Parameter Unit Standards Avg Avg Avg
Value Value Value
(2004-05) (2005-06) (2006-07)
Steam & SPM Mg/Nm3 500 Traces Traces Traces
Power
Generation
Plant SOX PPM 500 Traces Traces Traces
NOX PPM 100 34 39.19 32

91. ANALYSIS OF STACK EMISSIONS
(HRSG OF POWER PLANT)
Plant Parameter Unit Standards Avg Avg Avg
Value Value Value
(2004-05) (2005-06) (2006-07)
Heat SPM Mg/Nm3 500 Traces Traces Traces
Recovery
Steam
Generation SOX PPM 100 Traces Traces Traces
Plant
(HRSG)
NOX PPM 100 48 34.49 32

92. AMBIENT AIR QUALITY
Location SPM NH3 SO2 NO2
Unit Microgm/n Microgm/n Microgm/n Microgm/n
m3 m3 m3 m3
Standards(UPPCB) 500 100 120 120
NAAQS 360 100 80 80
Ammonia Storage 182 40 1.84 5.83
Area (Plant)
Guest House 176 32 2.00 4.52
(surrounding area of
plant)
GET Hostel 181 31 2.19 4.99
(surrounding area of
plant)
Transport Office 203 42 1.48 4.11
(surrounding area of
plant)

93. Ground Water Monitoring
Parameters Unit Standard Annual
Average
Analysis
Nitrate as NO3 PPM 10 1.49
Chromium PPM 0.1 NT

94. Hazardous Waste
Hazardous Waste Financial Year-2005-06 Financial Year-2006-07
a)From Process 20 m3 21 m3
Spent Oil(Reclaimed & ZNO:22.93 MT NIL
Reused /sold) Ni-Catalyst:3.81 MT
•Spent Catalyst
b)From Pollution
Control
Facilities
•Acidic and Alkaline
effluents Neutralized 35-40 m3/hr (Annual 35-40m3/hr(Annual
(Quantity) Average) Average)
21 m3 spent oil sold to m/s Friends Petro chemical Industires,Panipat
having authorisation from CPCB
21

95. SOLID WASTES
Hazardous Waste Financial Year(2005- Financial Year(2006-
06) 07)
Chromate sludge Use of Cr+6 Use of Cr+6
containing compounds has been compounds has been
Hydroxides of Fe, Al, discontinued since discontinued since
Cr, Zn & Calcium march 1999,Hence march 1999,Hence
there is no chromate there is no chromate
sludge formation sludge formation
•Quantity reused NIL NIL

96. LIQUID WASTES
(A)COOLING TOWER BLOW DOWN (125 M3/Hr.per plant)
(B ) OIL CONTAINING WATER (5 TO 10 M3/Hr):
C) ACIDIC AND ALKALINE WASTE (Avg. 35 – 40M3/Hr)
(
COST OF POLLUTION CONTROL MEASURES AGAINST PER
MT OF UREA PRODUCTION DURING 2006-07.
Rs. 25.80 (Approx )

97. ACTIVITIES FOR ENVIRONMENTAL PROTECTION WHICH IS
RELATED TO POLLUTION CONTROL
•Plantation of approx. 8,000 trees in year 2007-08 for gap filling
and replenishment of dead wood trees in factory and township
area.
Pre/Post monsoon “Monitoring of Underground Water” at different
locations as per CPCB guidelines.
Utilisation of more “Treated waste water in Green Belt”.
Consumption of “Natural Resources more economically”.
Safe Disposal of “Solid Waste.”
Implementation of Carbon Dioxide Recovery Unit (CDR)
A carbon Dioxide Recovery (CDR) unit has been installed in the
Capacity Enhancement / debottlenecking of the IFFCO Aonla Unit
, for which environmental clearance from U.P.Pollution Control
Board and Ministry of Environment & Forest have been obtained.
In this unit, a total of 450 MTPD of CO2 is recovered from the
stack flue gas of Primary Reformer of Ammonia –I . This quantum
of CO2 is utilised for the full conversion of ammonia to urea.

98. MEASURES TAKEN FOR ENVIRONMENTAL PROTECTION AND POLLUTION
CONTROL IN IFFCO AONLA UNIT
The environmental management at our unit aims for the abatement of pollution at the
source of generated itself. The following measures are being taken regularly for the
control of pollution and protection of environment :-
•Zero effluent technology, based on recycling and reuse of waste generated in the main
plants.
•Utilization of resources prudently so that waste generation is minimized.
•Treatment of waste water containing Ammonia & Urea through Deep Urea Hydroliser in
both the Urea Plant separately and reusing it as Boiler Feed Water.
•Treatment of Process Condensate by Process Condensate Stripper in both the
Ammonia Plant and reusing it as Boiler Feed Water.
•Treatment and polishing of Turbine Condensates from ammonia and urea plants in DM
Plant and reusing it as Boiler Feed Water.
Collection of Oil containing water and spilled oil from the compressor houses of all the
plants separately in oil collection pit. The oil is separated through “Disc Oil Separator”.
The reclaimed oil is either reused or sold to vendors having authorisation from CPCB
and the waste water is being sent to ETP for further treatment.
Neutralisation of Acidic and Alkaline waste generated due to the regeneration of
exhausted cation and anion resins in DM Plant.
Use of Eco-friendly, Non-chromate based corrosion inhibitor in cooling water
treatment. Thus avoiding the generation of hazardous Chromate sludge .
Treatment of occasional waste water containing ammonia generated during upset and
startup/shutdown condition of the plants in Effluent Treatment Plant through Air/Steam

99. •The treated waste water is collected in two nos. of LDPE lined lagoons (Guard-Ponds)
of capacity 85,000 m3 each at the terminal end of ETP. 60-70% of this treated effluent
is being used in the irrigation of green belt in and around the plant.
•Continuous monitoring of quality of liquid effluent, storm drain water, ground water,
stack flue gases, urea prill tower dust emission, ambient air by IFFCO’s own
Environmental Laboratory and also by an accredited third party U.P. Pollution Control
Board, Bareilly.
•All pollution control devices in the plants are maintained in perfect good condition and
their performances are monitored regularly by our laboratory.
•Built in safety logic’s and guards in the plant operations and safe shut down/starts ups.
•Education and training of employees regarding environmental issues.
•Generating awareness for Environment Protection in surrounding villages.
•The safe disposal of wastes of township households , plant canteen and Horticulture
and it’s conversion into manure by “VERMI-COMPOSTING PLANT”.
.The spent oil and spent catalysts (as and when discarded or exchanged) are
stored in factory premises in sealed covered drums on pucca plateform under a shed
and sold to vendors as per CPCB guidelines .
GREEN BELT DEVELOPMENT
Green belt has been developed all along the factory and township. The width of green
belt various from 80 M to 250 M as per the condition of environmental clearance.
Moreover additional afforestation is being carried out every year to fill up left out area
and replacement of dead wood trees in factory and township.

100. EMS IMPLEMENTATION :
IFFCO Aonla fertilizer complex (Plant & township) was accredited for ISO:14001: 1996
certificate by M/s BVQI in 12.08.2000. It was further recertified in January,2003 for 3
years. The ISO:14001:1996 was upgraded as ISO:14001:2004. Environment
Management systems of IFFCO Aonla Unit was also updated as per revised
ISO:14001:2004 standards and got certified by M/s BVQI in April,2006.
Now, the Environment Management System of IFFCO Aonla Unit is accredited by M/s
NQA-QSR and the certificate of ISO:14001:2004 is valid upto 15th May,2010.
OHSAS Accreditation:
The Occupational Health & Safety Management Systems of IFFCO Aonla Unit was
assessed by M/s NQAQSR and found to conform to the “Occupational Health & Safety
Systems Specification” i.e. OHSAS 18001:1999 – Amendment 1:2002 and awarded
IFFCO Aonla Unit with OHSAS:18001:1999 Certificate. The certificate is valid up to
08/12/2010.
AWARDS:
•INDO GERMAN GREENTECH ENVIRONMENT EXCELLENCE AWARD 1999-2000 &
2000-2001
IFFCO Aonla Unit has been assessed and awarded 1st and 2nd position for its
outstanding achievements in the field of environmental protection by Indo-Greentech
Foundation for two successive years i.e. 1999-2000 & 2000-2001 respectively.

101. •TERI CORPORATE ENVIRONMENTAL AWARDS 2002/03
IFFCO Aonla Unit has been awarded by “TERI” CORPORATE ENVIRONMENTAL
AWARD 2002/03 (CERTIFICATE OF PARTICIPATION) in recognition of it’s leadership
efforts towards environmental management and sustainable initiatives amongst
corporates with turnover above 500 crore rupees.
•GOLDEN PEACOCK ENVIRONMENT MANAGEMENT AWARD 2005
The Environmental Management Systems and techniques adopted in IFFCO Aonla Unit
were adjudged by a jury of World Environment Foundation and awarded “GOLDEN
PEACOCK AWARD - SPECIAL COMMENDATION” of Environment Management
Award-2005 in June, 2005.

102. ENVIRONMENTAL STATEMENT
•No adverse environmental impact observed in Eco-system due to plant
operation.
•All the pollution Control devices in plants are being kept in perfect
working condition and their performance is being monitored regularly.
•Network of irrigation piping has been laid down in plant and township to
utilise treated waste water/effluent . Approx. 60 to 70% of it is being
used in irrigation of green belt in and around the factory and township.
•Ammonia and Hydrogen monitoring system has been installed in the
plants for early leak detection of leakage’s, if any.
•Series of lectures are being taken regularly on environmental
awareness for the employees, contractors staff etc.
• Eco-friendly , Non-chromate corrosion inhibitors are being used in
cooling water treatment. Thus avoiding generation of hazardous waste
chromate sludge.

103. POLLUTION CONTROL IN UREA PROCESS

105. BLOCK DIAGRAM OF EMISSION SOURCES

106. Urea Process generates process water containing NH3-6%,CO2-2% &
Urea-1.0% by weight.
The principal source of this water is the synthesis reaction whwre 0.3 tonnes of
water is formed per ton of Urea.
2NH3+CO2→CO(NH2)2+H2O
The other sources of water are ejector steam,flush and seal water and steam used
in the waste water section.
The principal sources of urea ,NH3 and CO2 in the process water are:-
a)Presence of Ammonia in the urea solution feed to the evaporator
b)The formation of Biuret and the hydrolysis of urea in the evaporators,both
liberating NH3
2CO(NH2)2 →H2NCONHCONH2+NH3
CO(NH2)2+H2O →2NH3+CO2
c)Direct carry over of Urea from the evaporator separators to the
condensers(Physical entraiment)
d)The formation of NH3 from the decomposition of Urea ti Isocyanic Acid
CO(NH2)2 →HNCO+NH3
The reverse reaction occurs on cooling the products in the condensers.
(e) Off-gases from the recovery/recirculation stage absorbed in the process water.
(f) Off-gases from the synthesis section absorbed in the process water.
(g) Flush and purge water from pumps.
(h) Liquid drains from the recovery section.

107. Treated water : Urea-5 ppm,Ammonia-30 ppm
The purpose of the water teatment is to remove Ammonia,CO2,and Urea from the
process water and recycle the gases to the synthesis.This ensures raw material
utilisation is optimised and effluent is minimised.
Prill Tower Emissions
The prill tower is a major source of emission in urea plants. The large volumes of
discharged untreated cooling air contain particulate urea dust (1-2kg/t) as well as
NH3 (0.7-1.0kg/t).
Causes of dust formation

108. Cause Particle Size Dust %of
Range Total
Condensation products of urea vapours/aerosols 0.5-2.0µm 50
Reaction product of NH3 and isocyanic acid 0.1-3.0µm 20
(HNCO) to form Urea
Prill satellites and undersize prills 10-100µm 5
Crushing, abrasion and attrition on the tower floor 1-100µm 5
Seeding dust 1-20µm 20
Towers with natural draft cooling are reported to have less dust emission than
towers with forced/induced draft air cooling.
The lower air velocity and product mass per m 3 of tower volume reduces attrition
and carryover in the natural draft towers.
Operation and maintenance items significantly affecting dust formation
•Fouling of the prilling device causing wider spread in prill granulometry.
•High melt feed temperature causing increased evaporation.
•High prill temperature at the tower base. The largest prills may not have solidified
sufficiently and will fracture on impact.
•Dust emission is approximately proportional to prilling tower capacity.
•High air velocities and the air velocity distribution cause coarse dust to be
entrained.
•Weather conditions e.g. relative humidity, temperature can affect the air
quality/quantity.
•Unequal pressure in the prilling device causing a broad spread of prill size.

109. Prill tower emission abatement
Selection of the appropriate equipment for existing plants can be a complex issue.
Dry dust collectors, irrigated electrostatic
precipitators and irrigated dust scrubbers have been considered for dust
abatement but few have been commercially proven
. Wet scrubbers seem to be more attractive than dry dust collectors. Recovery of
the NH3 from the emission (for example by
aqueous scrubbing) is very inefficient due to the low partial pressure of the gas
in the discharged air.
Existing prilling plant performance
Prill Tower (Not Scrubbed) Urea Dust NH3
mg/Nm3 kg/t Mg/Nm3 kg/t
35-125 0.5-2.2 35-245 0.5-2.7
Causes of dust formation
The following reflects some speculations about the causes of dust formation .
•Urea vapour formation during hot spraying of the urea melt and its subsequent
condensation/solidification into small
•(0.5-3.0mm) particles. The vaporisation becomes negligible when the melt
concentration is reduced to 95%.
•Reaction product of NH3 with isocyanic acid to form Urea.
•Entrainment of fine dust in the air.

110. •Solidification of sprayed molten urea droplets prior to coating due to excessive
• air flow.
•High vapour pressure of sprayed molten urea.
•High or low temperature, producing soft or brittle granules.
•Inter-granular friction causing surface abrasion
Feasible and Available Emission Abatement Techniques
Gaseous emissions
•Scrubbing of off-gases with process condensate prior to venting inerts to
Atmosphere.
•Wet scrubbing of prill tower and granulation air to recover urea and NH3.
•Connection of ammonia pump safety relief valves/seals to a flare; connection of
• tank vents to the plant main stack
• or other safe location.
•Impact of granules with the metal surface of the drum.
•Dust reduction by producing granular rather than prilled product.
•Bag filtration of dust laden air from transfer points, screens, bagging
machines, etc. coupled with a dissolving system for recycle to the process.
•Flash melting of solid urea over-size product for recycle to the process.
•Collection of solid urea spillages on a dry basis
Liquid emissions
Treatment of process waste water for recovery of urea, NH3 and CO2.
Improved evaporation separator design to minimize urea entrainment.
Provision of adequate storage capacity for inventory to cater for process upset
and shut-down conditions.

111. •Provision of submerged tanks to collect plant washings, etc. from drains for
recycle to the waste water treatment section.
•Use of mechanical seals instead of gland packing for pumps.
•Use of closed circuit gland cooling water system for reciprocating pumps.
•Replacement of reciprocating machinery with centrifugal type.
Solid waste
In the modern urea processes although the sophisticated handling of product
urea has reduced the chances of spillage,
still the formation of lumps and some spillage of urea prills cannot be ruled out.
To meet this exigency, a urea melting
system to employed. The melt urea obtained from the spillages and sweeping
should be suitably recycled in the processes.
Ambient Air Limit
500 µ g / NM3
SPM
120 µ g / NM3
SO2
NO2 120 µ g / NM3
NH3 400 µ g / NM3

112. Stack Limit
50 mg / NM3
Urea
NH3 50 PPM
Prill Tower Limit
NOx 100 PPM
SOx 500 PPM
CO 50 PPM
SPM 500 PPM

113. Effluent Discharge Limit
MINAS Norms UPPCB Norms
PH 6.5-8.0 5.5-9.00
colour absent absent
NH3 (Total) 50 PPM 100
Free NH3 4 PPM 5 PPM
TKN 100 PPM 150 PPM
COD 250 PPM 250 PPM
BOD 30 PPM 30 PPM
Cl- 600 PPM 600 PPM
Oil & grease 10 PPM 10 PPM
TSS 100 PPM 100 PPM
Cr (Cr+6) 0.1 PPM 0.1 PPM
Po4- - 5 PPM
Zn - 5 PPM
V+5 - 0.2 PPM

114. Raw Water Analysis
PH 8.1
CONDUCTIVITY 560
TH 44
Ca AS Caco3 ppm 29
Mg as CaCo3 ppm 15
P. Alk as CaCo3 NT
M Alk as Ca Co3 219.25
Cl as Cl 17.73
Sulphur as so4 37.03
Iron as Fe 0.08
Silica as Sio2 20
T..D.S 302
Turbidity NTU <1.0
Sodium as Na 106
Nitrite as NO3 0.30

115. CARBON DIOXIDE RECOVERY (CDR) FROM FLUE GASES OF PRIMARY
REFORMER AT IFFCO AONLA UNIT
IFFCO, a premier fertilizer company has installed and commissioned Carbon
Dioxide Recovery (CDR) Plant at it‟s Aonla & Phulpur Units for recovery of CO2
from Primary Reformer Flue Gases based on the technology from M/s Mit
subishi Heavy Industries (MHI) Limited, Japan and Detailed Engineering from M/s
Tecnimont ICB (TICB) Private Limited, Mumbai.
The CO2 recovered from flue gases makes up for deficit of CO2 due to use of Lean
NG / R-LNG & leads to conversion of all the Ammonia produced to Urea, thus
avoiding Ammonia stock build up. The recovery of CO2 from flue gases also
reduces CO2 emissions (Green house gas) to atmosphere and thus contributes to
cleaner environment.
Carbon Dioxide (CO2) Recovery from Flue Gases.
The CO2 Recovery from flue gases is having following distinctive advantages:
It reduces CO2 emissions (Green house gas) to atmosphere, contributes to
cleaner environment, conserves carbon intensive fossil fuels like Naphtha and
thus has a great potential to be covered under Clean Development Mechanism
(CDM) of UNFCCC. The trading of certified emission reductions (CERs) through
CDM generates additional revenues & increases the viability of the CDR Project.

116. Production of additional CO2 from CDR unit in place of costlier Naphtha feed,
shall decrease cost of production of Urea and hence shall reduce Government
of India‟s annual subsidy outgo.
SALIENT FEATURES OF CDR PROJECT
The following are the salient features of CDR Project ordered on M/s TICB,
Mumbai & M/s MHI, Japan :
Source of CO2 : Flue gases from Primary Reformer stack of
Ammonia Plant
Plant Capacity : 450 MTPD CO2 (100% basis)
MHI CDR
PROCESS
The CDR plant consist of four main sections; 1) Flue gas pre-treatment section,
2) CO2 absorption section, 3) Solution regeneration section, 4) CO2 compression
section. The following block flow diagram shows the plant configuration.
TREATED
FLUE GAS
CO2 LEAN
SOLUTION
Flue Gas Source FLUE (1) (2) (3) (4)
(Primary GAS Flue Gas CO2 Solution CO2
Reformer) Pretreatment Absorption Regeneratio Compressio
n n CoCO2 Product
2 product
CO2 RICH fnfp’I’I’
SOLUTION To Urea
Plant

118. •1) Flue Gas Pre-treatment
The hot flue gases at about 150 – 180 0C are cooled to 42 0C, using flue gas
cooling system prior to the CO2 absorption in Absorber, to optimise KS-1
solution consumption & lower flue gas temperature which is favourable for
CO2 absorption.
The Flue gas water cooler is a packed column with SS structured packing.
Flue gas is cooled in the upper packing section of the Flue gas water cooler
by direct contact with water supplied from top of the tower. Circulating water
is cooled by a plate type heat exchanger. De-SOx (SOx removal) is carried out
in the lower packing section of Flue gas water Cooler by circulating dilute
caustic solution. Any slippage of SOx in the Flue gas from Flue gas water
cooler to CO2 Absorber shall cause KS-1 Solvent degradation.
A Flue gas blower has been provided at downstream of Flue gas water cooler
to draw the flue gas from existing stack to overcome the pressure drop
across Flue gas water cooler & CO2 Absorber.
•2) CO2 Absorption
The CO2 absorber is a packed bed column with SS structured packing. The CO2
absorber has two main sections namely, the CO2 absorption section in the lower
part, and the treated flue gas washing section in the upper part.
•The cooled flue gas from the Flue gas water cooler is introduced into the bottom
section of the CO2 absorber through flue gas blower. The flue gas comes in
contact with the KS-1 solution on the surface of the packing in absorption section,

119. where CO2 in the flue gas is absorbed by the KS-1 solution. The flue gas then
moves upward into the treated flue gas washing section in the upper part of the
CO2 absorber . The flue gas comes in contact with water for washing of entrained
amine content, as well as for cooling down to maintain water balance within the
system. The treated flue gas is exhausted from the top section of the CO2
absorber at sufficient height.
Rich solution from the bottom of the CO2 absorber is pumped to the Regenerator
through Solution heat exchangers to exchange heat with hot lean solution from
Regenerator bottom.
•3)Solution Regeneration
The Regenerator is a packed column with random SS packing, where the rich solution is
steam-stripped and CO2 is removed from the rich solution.
The rich solution (from the bottom of the CO2 absorber) after exchanging heat with the hot
lean solution (from bottom of regenerator) in “Solution heat exchangers” enters the upper
section of the regenerator. The regeneration heat is indirectly supplied by LP Steam
through re-boilers.
The overhead vapor from Regenerator column is cooled to 40C in Regenerator
condenser using cooling water. The condensed water is returned from the Regenerator
reflux drum to the top of the Regenerator by the Regenerator reflux pump to enhance
CO2 purity, remove KS-1 mist entrained in CO2 gas & maintain water balance in the
system .

120. The lean solution is cooled to the optimum reaction temperature of 40C by the
Solution heat exchangers and the Lean solution cooler prior to being fed to the CO2
absorber. 10% of the lean solution flows through a carbon filter system to eliminate
oil and soluble impurities. The mechanical guard filters are provided before and
after the carbon filter to remove insoluble particulate.
•4) CO2 Compression
The CO2 product gas is compressed by the CO2 compressor & then cooled in a
Compressor discharge cooler to supply product CO2 at a pressure of 0.8 Kg/cm2g
& temperature of 40 C at CDR plant battery limit. The product CO2 having purity
around 99.8 %(v/v) is sent to the existing Urea Plants by interconnection with
existing CO2 header.

121. ENVIRONMENTAL POLICY OF IFFCO AONLA
IFFCO Aonla unit is committed for continual improvement and protection of
environment by setting and reviewing the objectives and targets through
Environmental Management System focussing at: :-
•Compliance of applicable legislation at work place and other
requirements, which the organization subscribe.
•Monitoring and conserving natural resources.
•Effluent and waste minimization by way of recycling and reuse.
•Developing awareness and competence amongst Employees,
Contractor’s Staff and related agencies on environmental issues.
•Emergency preparedness for safety of concerned personnel and plant.

122. Achievement of Objective & Target of 2006- 07
No.1. To achieve Urea spillage not more than 397 MT/Month in 2006-07 by
reducing 5% of the value achieved in 2005-06 i.e 418 MT/Month.
Achieved 390 MT/Month Urea Spillage in year 2006-07.
2.To reduce water consumption below 6.70 M3/MT of urea production in year 2006-
07.
Achieved 5.40 M3/MT Urea Production in year 2006-07.
•To plant minimum 10,000 trees in plant and township.
10285 Trees planted during year 2006-07 in plant and township.
•To keep SPM particulate matter in ambient air below 200 micrograms/nm3 in plant.
Achieved annual average value of SPM in Plant 181.75 Microgram/NM3.
•To bring awareness among new / transferred employees, contractor’s staff and
related agencies on relevant environmental issues to minimum 200 participants.
Imparted awareness on environmental issues to 200 participants.

123. Environmental Aspects Analysis Criteria :G = AxBxCxDxExF
Point Quantity Occurrence Impact Legislation Detection Control
(A) (B) (C) (D) (E) (F)
5 Excessiv Continuous Human Not More than Absence
e Health Meeting 24 hours
4 High Daily Flora Within 24 Mechanis
Fauna hours m
and Provided
Global
issue
3 Medium Once a Resource Not Within 8 Human
Week Depletion meeting Hours Interventio
Company’s n
Threshold
Limit
2 Low Once a Cause Within 1 In built
month Discomfor Hours secondary
t Control
1 Negligibl Very Rare Negligible Complianc Immediatel Available
e e y &
Effective

124. AMBIENT AIR QUALITY STANDARDS IN RESPECT TO NOISE
Sr.No. Activit Category of Day Time Night Time Applicable
y Area/Zone (6AM to (10PM to 6 Section of
10PM) AM) Rules
1.0 (A) Industrial area 75 70 Schedule as
per rule 3(1)
2.0 (B) Commercial 65 55 & 4(1) The
area Noise
3.0 © Residential 55 45 Pollution
area Rules, 2000
4.0 (D) Silence zone 50 40

126. Journey from barren land
to
large and eco-friendly
fertiliser complex

127. Aonla site in 1984
( Land acquisition )

128. Aonla site in 1988
( Aonla-I commissioned )

129. Aonla site in 2007
( Large & eco-friendly fertiliser complex )

130. N.P.RAO