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CENTURY PULP AND PAPER

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Title: CENTURY PULP AND PAPER


1
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2
CENTURY PULP AND PAPER
LALKUA, NAINITAL
( A BK BIRLA GROUP OF COMPANY ) ISO 9001
2000 AND ISO -14001 CERTIFIED COM PANY
  • AN INTEGERATED PULP PAPER UNIT
  • 31320 TPA RAYON GRADE UNIT
  • 37250 TPA WOOD BASE WRITING PAPER
  • 84600 TPA BAGASSE BASE PAPER

ECO MARKED BAGASSE PAPER
3
CENTURY PULP AND PAPER POWER ARRANGEMENTS
  • 6.8 MW TG SET
  • 21 MW TG SET
  • 7.5 MVA CONTRACT DEMAND FROM
  • UPCL

6,10,000 UNITS /DAY
4
CENTURY PULP AND PAPER THERMAL ENERGY
ARRANGEMENTS 23 TPH 46 Kg/cm2 FBC C F B
3 NO 25 TPH 46 Kg/cm2
SPREADER STOCKER CFB 1 NO 50 TPH 62 Kg/cm2
FBC C F B 2
NO 40 TPH 46Kg/cm2 CHEM REC BOILER( BHEL ) 1
NO 50 TPH 62Kg/cm2 CHEM REC BOILER( ABL ) 1
NO
5
(No Transcript)
6
ELECTRICAL ENERGY (KWH) 2001 - 2004
7
  • ELECTRICITY CONSUMPTION AND COST

  • 2001-02 2002-03 2003-04
  • PURCHASED
  • UNITS (Lac kwh/yr) 239.83
    192.27 159.73
  • COST ( Rs lacs/yr) 1399
    1177.84 746.84
  • OWN GENERATION
  • THROUGH DG SETS
  • UNITS (Lac kwh/yr) 47
    34.81 19.37
  • COST ( Rs lacs/yr ) 219.44
    182.88 117.13
  • THROUGH STEAM TURBINES
  • UNITS ( Lac kwh/yr) 1754.58
    1865.88 2001.13
  • COST ( Rs lacs/yr) 1937.58
    1974.96 1903.86

8
TOTAL CONSUMPTION OF ELECTRICITY
2001-02 2002-03
2003-04 UNITS (Lac kwh/yr ) 2041.41
2092.96 2180.23 COST (Rs lac/yr)
3556.02 3335.68 2767.83
9
  • THERMAL ENERGY CONSUMPTION FOR PROCESS

  • 2001-02 2002-03 2003-04
  • COAL
  • HEAT VALUE (Mkcal/yr) 728037 653007.6
    651336.7
  • BLACK LIQUOR
  • HEAT VALUE 659445
    704815 711616.75
  • PITH
  • HEAT VALUE 60501
    78867 74641.5
  • TOTAL 1447983
    1436690 1437595

10
  • APPROACH FOR ENERGY CONSERVATION
  • AWARENESS EDUCATION TRAINING
  • CAPACITY UTILIZATION INCREASED
  • OPTIMIZATION OF VOLTAGE
  • OPTIMIZATION OF FREQUENCY
  • OPTIMIZATION OF OPERATING PROCEDURES
  • THRUST ON RECYCLE WASTE MINIMIZATION
  • FINE TUNING OF PLANTS EQUIPMENTS
  • INSTALLATION OF VFDS
  • ADOPT ENERGY EFFICIENT LIGHTING
  • USE OF EFFICIENT EQUIPMENT
  • TECHNOLOGY UPGRADATION
  • ASSESSMENT AND MONITORING

11
ASSESSMENT MONITORING
  • AUDIT CONDUCTED BY CII APRIL2003
  • 39 ENERGY SAVING SCHEMES IDENTIFIED
  • AUDIT CONDUCTED BY INGERSOLL RAND SEPT 2003
  • 8 SCHEMES IDENTIFIED
  • AUDIT CONDUCTED BY ECKO PUMPS FOR PAPER
  • M/C III VACUUM SYSTEM OCT2004
  • 4 SCHEMES IDENTIFIED
  • AUDIT CONDUCTED BY DSCL FOR ENERGY COST
  • REDUCTION IN FEB 2004 4 SCHEMES
    IDENTIFIED
  • MOTOR EFFICIENCY ASSESSMENT BY VBI SYSTEMS
  • PLANT TECHNICAL AUDITS BY INDEPENDENT
  • COUNSULTANTS AUG 2004

12
ORGANISATIONAL SET UP FOR ENERGY CONSERVATION
PRESIDENT
EC CELL
LOSS IDN COM
ISO 14001/ ISO 9001/QC
TPM
PRODUCTION TPM SEC 3
MEMBERS MR. POWER HOUSE
PILAARS CROSS FUNCT SYSTEM
COORD.
TEAMS
ELECTINST OVERLAPPING
QUALITY CIRC

COMMITTEES ENV
WATER STO PUR PURTA
13
  • ENERGY CONSERVATION CELL
  • FUNCTIONS
  • COORDINATE STEAM POWER REQUIREMENTS
  • STUDY VARIANCE
  • IDENTIFY ENERGY CONSERVATION OPPURTUNITIES
  • REVIEW ENERGY AUDIT FINDINGS
  • STRATEGY
  • INCREASE AWARENESS
  • ACHIEVE MAXIMUM PLANT EFFICIENCY
  • INDUCT LATEST TECHNOLOGY
  • ENSURE TIME BOUND IMPLEMENTATION

14
TPM
A ZERO BASED APPROACH
ENHANCE PLANT EFFICIENCY
15
ZERO BASED APPROACH
LOSS FAILURE DEFECT DOUBT ACCIDENT BREAKDOWN
0
16
AUTONOMOUS MAINTENANCE( JISHU HOZEN )
MY MACHINE I MAINTAIN
17
EDUCATION AND TRAINING
  • SKILL DEVELOPMENT TRAINING PROGRAMME
  • TPM AWARENESS 118
  • TECHNICAL 722
  • BEHAVIORAL 99
  • FIRE AND SAFETY 209
  • ON JOB TRAINING THROUGH
  • ONE-POINT-LESSON
    SHEET

18
TPM RE- DEFINED
TOTAL POSITIVE MIND
TOTAL POSITIVE MIND
TOTAL POSITIVE MIND
19
  • LOSS IDENTIFICATION COMMITTEE
  • HIGHLIGHT PROCESS INEFFICIENCIES
  • CHECK LOSSES OF ALKALI,FIBRE,WATER,
  • CHEMICAL AND STEAM
  • ARRANGE CORRECTIVE MEASURES

20
  • ISO 9001-2000
  • CONTINUAL IMPROVEMENT
  • WASTE MINIMIZATION
  • ISO14001
  • CONSERVATION OF RESOURSES
  • ADOPTING CLEANER TECHNOLOGIES
  • ALTERNATIVE FIBRE RESOURSES
  • UTILIZATION OF WASTE LIME MUD
  • UTILIZATION OF WASTE PITH
  • QUALITY CIRCLE
  • 19 CIRCLES OPERATIVE

21
ANNUAL SAVING IN POWER UTILISATION WITHOUT
INVESTMENT
S.NO. SCHEMES INVESTEMENTS (Rs IN LACS) SAVINGS (Rs IN LACS)
1. REDUCED TG FREQUENCY 0 76.20
2. OPTIMISE TG VOLTAGE 0 3.62
3. OPTIMISE RGP VOLTAGE 0 2.49
4. PUT OFF 12.5 MVA TR SET 0 3.02
TOTAL TOTAL 0 85.43
22
NO / LOW INVESTMENT SCHEME
2001-02
2002-03 2003-04 NO OF SCHEMES
2 8
9 SAVINGS / ANNUM KWH (LACS)
11.82 8.914 36.755
COAL EQ (TONS) - 16366
32550 Rs ( LACS) 24.65
312.45 658.64 INVESTMENT
2.11 -
-
TOTAL Rs 995.74
23
ENERGY CONSERVATION SCHEMES NO / LOW
INVESTMENT
( 2001 02)
SN PROJECT ANN SAVINGS ELECT ANN SAVINGS ELECT ANN SAVINGS THERMAL ANN SAVINGS THERMAL INVESTMENT
SN PROJECT KWH (LACS) RS (LACS) EQ COAL RS (LACS) INVESTMENT
1 Reduction of distribution losses by optimizing voltage of MCC 1.9 3.8 - - 2.11
2 Reduction of running hours. Foam breaker Worthington Pump Fresh water pump Blow tank pump 0.79 6.06 2.45 0.62 1.58 13.12 4.91 1.24 - - - - - - - - 0 0 0 0
SUB TOTAL 11.82 24.65 - - 2.11
24
ENERGY CONSERVATION SCHEMES
NO / LOW INVESTMENT ( 2002 03)
SN PROJECT ANN SAVINGS ELECT ANN SAVINGS ELECT ANN SAVINGS THERMAL ANN SAVINGS THERMAL INVESTMENT
SN PROJECT KWH (LACS) RS (LACS) EQ COAL RS (LACS) INVESTMENT
1 Reduction of combustion air in Boiler no 2,3,56 4.62 9.25 940 16.92 0
2 Reduction of PA Header Pressure in Boiler NO.2,3,5 6 2.48 4.96 - - 0
3 Optimization of FBC Boiler operation by reducing the bed hight and control of FD air - - 13680 246.2 0
25
NO / LOW INVESTMENT ( 2002 03)
4 Minimum flow lines of old feed pump 34connected to Dearator instead of DM Tank resulting in savings of energy 0.17 0.37 - - 0
5 By pass arrangement on Solcon Crusher for segregation of 25 mm Coal for B4 resulted in power saving 0.014 0.028 54 0.972 0
6 Vent steam of Dearators utilized for heating Boiler feed water - - 1667 30.0 0
7 Elimination of 3 Audco valve after secondary black liquor heater in firing line, reducing oil consumption - - 25.0 0.50 0
26
NO / LOW INVESTMENT ( 2002 03)
8 Replaced Reciprocating feeder by Vibro feeder in BC-I resulting in reduced running hours 1.63 3.25 3.25 - - - 0
SUBTOTAL 8.914 17.858 17.858 16366 294.592 294.592 0
(2003 04 ) (2003 04 ) (2003 04 ) (2003 04 ) (2003 04 ) (2003 04 ) (2003 04 ) (2003 04 ) (2003 04 )
1 Control of super heater Safety Valve Blowing by Automation of combustion control logic in Boiler no 5 6 - - - 109 1.96 0 0
2 Optimize LT Voltage in RGP 1.2 1.2 2.4 - - 0 0
3 Recovery of flash Steam from CBD tank of Boiler - - - 41 0.74 0 0
27
NO / LOW INVESTMENT ( 2003 04)
14 Arresting air leakage of B6 pre heater and bellows resulting in reduced fan consumption 4.8 9.6 - - 0
15 Use of Cooling Tower Blow Down for submerged ash conveyor 0.545 1.09 - - 0
16 Optimization of voltage for Transformer 309 1.4 2.8 - - 0
17 Optimization of voltage for Transformer 307 0.3 0.6 - - 0
18 ESP Heater connection modification 0.51 1.02 - - 0
19 Optimization of captive generation 28 56.0 32400 583.00 0
SUBTOTAL 36.755 73.51 32550 585.73 0
28
VARIABLE FREQUENCY DRIVES
29
  • ENERGY CONSERVATION SCHEMES
  • VFD
    2001-02 2002- 03 2003-04
  • TOTAL NOS INSTALLED 16
    11 25
  • INVESTMENT
    39.3 8.06 31.03
  • SAVINGS /ANNUM
  • KWH (LACS)
    21.2 3.66 11.36
  • Rs (LACS)
    42.4 8.22 22.72

73 . 34 LACS
UNIT COST Rs 2.00
30
VFD - FANS, BLOWERS PUMPS
AFFINITY LAWS Q1 N1 Q2 N2
2 P1 N1 P2
N2 3 HP1
N1 HP2 N2
P2
P mtr of wc
P1
Q1
Q2
Q(LPM)
31
THROTTLING VS SPEED CONTROL
32
POWER REQUIREMENT VSD VS VALVE THROTTLING
  • A- damper control
  • 0.4 0.6Q
  • B -VSD control Q3
  • ASSUMPTIONS
  • Static Head on fan/
  • pump is negligible.
  • Fan/pump input is 0.4
  • Per Unit under full
  • valve/ damper
  • closed condition.

100
A
Fan/ Pump Input Power
80
60 40 20
B
.2 .4 .6 .8 1.0
Q(LPM) Per unit flow discharge
33
ENERGY CONSERVATION SCHEMES
ELECTRICAL VFD
(2001-02)
SN PROJECT ANN SAVINGS ELECT ANN SAVINGS ELECT INVESTMENT
SN PROJECT KWH (LACS) RS (LACS) INVESTMENT
1 (I) FD fan-boiler 2 4 (II) SA fan-boiler4 (III) DM transfer pump (IV) PA SA fan ABL BHEL boilers ID Fan new lime kiln (V) Fan pump sheeting m/c (VI) Bag st prep FW.HW pumps (VII) Blow tank diln pumps 19 38.0 35
2 VFD for Bag Brown Stock washer 1,2,3 2.2 4.4 4.3
34
ELECTRICAL VFD (2002-03)
3 Filter water pump no.2 0.46 0.92 0. 96
4 RGP (I) HP Pressure blower (II) Propeller pump (III) Blow TANK Cir Pump (IV) CPT stock pump 0.288 0.432 0.72 0.216 0.57 0.86 1.44 0.43 2.4 2.6 1.3 0.8
5 UTILITY (I) Table Feeder (II) Screw Conveyor (III) Tertiary Air fan (IV) EPH tank pump (V) SCBL pump (VI) MOL transfer pump 2.0 4.0 4.0
35
ELECTRICAL VFD (2003-04)
7 RGP (i)Hot water pump no. 3 (II) Wash water pump (III) UNBL 4 STOCK pump (IV)B1.4 stock pump 1.22 2.44 3.81
8 BAGASSE (i)Sweetner stock pp (II)Poly disc Feed pp (III)Long fibre feed pp to blending (IV) Broke feed pp to Blending 3.61 7.22 5.0
9 UTILITIES (I)ID FanB4 (II)ID Fan B5 12 (III) PA Fan B5 12 3.53 7.06 8.69
36
ELECTRICAL VFD (2003-04)
10 RGP Hot Water pp no3 Wash water pp UNBL 4 ST pp BL 4 ST pp 1.22 2.44 3.81
11 WPP Alkali b/w pp Hypo B/W pp Hypo ii B/W pp CLO2 B/W pp Alkali ST pp Secondary Fan pp M/CII Talcum pp III 1.78 3.56 9.72
37
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38
SLD BAGASSE PAPER M/C
39
SLD BAGASSE PULP
40
SLD RGP MCS
41
SLD WPP CCS
ETP TR 3
42
132/11 KV
10MVA 11/11KV
TG 2 21 MW
TG 1 6.8MW
BPULP B M/C RGP WPP
43
HARMONICS STUDY FINDINGS
TG1 TG2 DG
GR TR 1 GR TR 2 Vthd 1.93
3.80 2.98 0.72
1.78 Ithd 3.52 3.63
3.42 1.17
1.78 PERMITTED VALUES 5
44
  • OTHER ELECTRICAL SCHEMES FOLLOWED
  • PROVISION OF LOAD TRANSFER FROM GRID TO TG
  • WITHOUT INTERRUPTION TO UTILIZE SOURCES
  • PREVENT IDLE RUNNING OF EQUIPMENTS BY
  • INTERLOCKING OF PUMPS AGITATORS
  • EFFECTIVE CONTROLS LIKE ONE PB FOR
  • COMPLETE GROUP EQUIPMENTS OF PLANT
  • SWITCH OFF EQUIPMENTS THROUGH TIMERS
  • DELTA - STAR FOR LIGHTLY LOADED MOTORS
  • NEUTRAL COMPENSATORS FOR UNBALANCE LOADS
  • LEDS FOR INDICATING LIGHTS
  • LOW LOSS HRC FUSES
  • USE OF ENERGY SAVERS FOR LIGHTING CIRCUITS
  • USE OF PHOTO CELLS FOR STREET LIGHTS
  • SPLITTING OF CIRCUITS FOR BETTER CONTROL

45
TOTAL SAVINGS / ANNUM ( FOR LAST THREE
YEARS) KWH (LACS)
4.62 Rs (LACS)
9.24 INVESTMENT Rs (LACS)
9.65
46
ENERGY CONSERVATION SCHEMES
ELECTRICAL OTHERS
SN PROJECT ANN SAVINGS ELECT ANN SAVINGS ELECT INVESTMENT
SN PROJECT KWH (LACS) RS (LACS) INVESTMENT
1 Energy Efficient Controller for ESP 0.23 0.46 0.92
2 Replacement of High Loss Capacitors 0.22 0.44 0.4
3 Replacement of 132 Kw motor by 93 Kw motor for CLO2 compressor 1.20 2.40 1.3
4 Replacement of High Loss Capacitor 1.60 3.20 4.0
5 Replacement of 40 W tubes by 36 W 0.176 0.350 0.66
6 Use of Energy efficient Ballasts 0.173 0.346 1.44
47
ENERGY CONSERVATION SCHEMES
ELECTRICAL OTHERS
6 Installation of Neutral Compensators 0.51 1.02 0.51
7 Installation of Neutral Compensators New Evaporators 0.24 0.48 0.27
8 Replacement of Heat Exchanger by Blower For DC Motors 0.27 0.54 0.15
SUB TOTAL 4.62 9.24 9.65
48
TOTAL SAVINGS THERMAL / PROCESS 2001-02
2002-03 2003-04 INVESTMENT
77.55 78.90
853.79 SAVINGS KWH (LACS)
29.02 27.69 19.73 COAL
EQ.(TONS) 6765.7 5500
3593 Rs (LACS)
235.48 160.58 574.46
970.52
KWH Rs 2.00
COAL/TON Rs1800
49
ENERGY CONSERVATION SCHEMES
THERMAL / PROCESS 2001 - 02
SN PROJECT ANN SAVINGS ELECT ANN SAVINGS ELECT ANN SAVINGS THERMAL ANN SAVINGS THERMAL INVESTMENT
SN PROJECT KWH (LACS) RS (LACS) EQ COAL RS (LACS) INVESTMENT
1 Installation of Bl. Liq cooler - - 4000 72 50.0
2 High Eff. Pumps in WPP Pulp 2.4 4.8 - - 14.0
3 Interconnection of First Effect pumps of RGP WPP Evaporators 0.7 1.4 - - 0.5
4 Use of hot water in MOL preparation instead of Fresh Water - - 228 4.8 0.25
5 Replacement of MP Steam with LP Steam in Dregs Mixer 0.16 0.32 - - 0.10
50
THERMAL / PROCESS 2001 02
contd
6 Removal of one stage in HT Feed pump no 4 5 0.4 0.8 - - - 0.2
7 Reel Turn Up System on PM/C III to eliminate paper wastage during roll change 25.36 50.72 2537.7 2537.7 100.64 12.5
SUBTOTAL 29.02 58.04 6765.7 6765.7 177.44 77.55
2002 - 03 2002 - 03 2002 - 03 2002 - 03 2002 - 03 2002 - 03 2002 - 03 2002 - 03
8 Replacement of existing Black Liquor heater with new heater - 838 16.76 0.5
9 Replacement of Wet Ash handling system by Dry Ash handling system Radler conveyor for ESP Ash 3.15 6.30 6.30 - - 0.4
10 Replacement of MP steam seal with water seal in Evaporator PP - - - 419 8.38 2.00
51
THERMAL / PROCESS 2002 03
contd
11 High Efficiency Vaccum pumps in WPP 24 48 - - 63.0
12 BL Liq Pump to cooler Gravity slusher 2.6 5.20 - - 0.10
13 Increase Pith feeding to Boiler by change of screen size to 12 mm from 8 mm - - 2398 43.16 0.1
14 Replacement of LP steam LP Steam in oil Heater in Old Lime Kiln 0.4 0.8 - - 0.2
15 Replacement of steam Ejectors with Vacuum Pump in old Evaporator -3.36 -6.72 1845 36.9 12.3
16 Modifications of sec air distribution duct in Old Lime Kiln 0.9 1.80 - - 0.3
TOTAL 27.69 55.38 5500 105.2 78.9
52
THERMAL / PROCESS 2003 04
17 Installation of Sonic soot Blower in Boiler 4 - - 200 3.66 0.5
18 Installation of Efficient Liquor Circulation Pump in Digester 4 0.35 0.79 - - 10
19 Installation of Efficient Vacuum Pump in WPP Pulp mill 3.80 7.6 - - 10.0
20 Continuous Chemical Feed in Stock in WPP 7.12 14.25 - - 25.0
21 Installation of Efficient Vacuum Pump in WPP M/C 9.9 22.1 - - 37.0
22 Effective Blow Heat Recovery in WPP - - 2121 35.6 12.0
53
THERMAL / PROCESS 2003 04
contd
23 Surface Finishing of Paper M/C dryers - - 1272 21.4 52.0
24 Arresting air infiltration in BHEL ABL Boilers 1.5 3.0 - - 4.0
25 Installation of efficient liquor circ. pump 0.96 1.86 - - 17.0
26 Installation of Producer Gas Plant - - Fuel Subs 196 338
27 Installation of Wet Pith Screw Press -3.9 -7.8 Fuel Subs 134 348.29
SUB TOTAL 19.73 41.8 3593 388.7 853.8
54
1888.53
  • TOTAL ENERGY SAVINGS FOR
  • LAST 3 YEARS
  • 2001- 02
    2002- 03 2003- 04
  • NO OF MEASURES 8 34
    47
  • ( IMPLEMENTED )
  • INVESTMENT (LACS) 77.85 138.8
    893.85
  • SAVINGS ACCHIEVED
  • KWH (LACS) 38.94
    66.27 78.614
  • THERMAL (FUEL ) 11063 87900
    143608
  • ( MkCAL )
  • Rs LACS 205.61 541.17
    1141.75

55
RGP 44 PAPER 92
SPECIFIC POWER CONSUMPTION TREND
56
RGP 1.468 PAPER 1.346
SPECIFIC STEAM CONSUMPTION Mkcal / TON
57
  • INNOVATIVE SCHEMES
  • SUBSTITUTION OF FURNACE OIL
  • UTILIZATION OF SOLID WASTE
  • OPTIMIZATION OF GENERATION

58
ENERGY THROUGH RFO HIGH COST FUEL
PRODUCER GAS PLANT
RECALCINE
LIME
LIME SLUDGE
59
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60
ENERGY THROUGH COAL - LOW COST FUEL
PRODUCER GAS PLANT
RECALCINE
LIME
LIME SLUDGE
INVESTMENT Rs 338.0
LACS SAVINGS IN2003-04 Rs 196.0 LACS
61
BAGASSE STORAGE
62
DE - WATERING PITH PRESS
CONTINUOUS DIGESTER
WASHING
BAGASSE
WET PITH 80 MOISTURE
63
DE - WATERING PITH PRESS
BAGASSE
WASHING
CONTINUOUS DIGESTER
INVESTMENT Rs 348.29 LACS ANNUAL SAVINGS
Rs 134 LACS
DE WATERING PITH PRESS
50 MOISTURE PITH
64
(No Transcript)
65
OPTIMIZATION OF GENERATION POWER GENERATION
23.5 MW
130.6
70.65
B4
BH EL
B1
B5
B6
A BL
15.0
62
46
PRDS
110.5
68.94
21 MW
6.8MW
PRDS
27.28
PRDS
COND
33.17
80.75
4.7
3.5
3.5
15.8
37.41
2.5
PLANT
10.5
10.5
PLANT
PLANT
PLANT
66
OPTIMIZATION OF GENERATION POWER GENERATION
22.0 MW
133.4
50.6
B4
BH EL
B1
B5
B6
A BL
20.27
46
62
PRDS
111.2
68.94
21 MW
6.8MW
PRDS
23
PRDS
COND
33.42
73.43
3.36
3.5
3.5
2.0
14.71
35.52
PLANT
10.5
10.5
PLANT
PLANT
PLANT
67
OPTIMIZATION OF GENERATION
  • SAVINGS
  • FULL EXTRACTION AT 10.5 Kg/cm2 REDUCED
    PRDS FLOW
  • HIGHER STEAM FOR COGEN
    IMPROVED EFFICIENCY
  • REDUCED VENTING OF STEAM
  • STOPPED ONE CFB
  • DEARATOR STEAM REDUCED
  • ONE BOILER FEED PUMP STOPPED
  • LOAD ON COOLING TOWER REDUCED
  • COAL _at_2700MT/MONTH
    Rs 583 LACS
  • POWER _at_350 KWH
    Rs 56 LACS
  • TOTAL
    Rs 639 LACS

68
  • ENVIRONMENTAL MANAGEMENT
  • GREEN PRACTISES SYSTEMATICALLY ADOPTED
  • AND INTEGRATED INTO OVERALL PRODUCTION
  • PROCESS
  • ENZYMATIC PRE BLEACHING
  • BIO REFINING OF PULP
  • COOKING AIDS IN DIGESTER
  • FARM FORESTERY
  • CONSERVATION OF RESOURSES
  • SOLID WASTE MANAGEMENT

REQUIREMENT FOR CORPORATE RESPONSIBILITY FOR
ENVIRONMENT PROTECTION
69
WATER CONSUMPTION TREND
KL/TON
24
70
WATER CONSERVATION ACHIEVED THROUGH 23 SCHEMES
IMPLEMENTED IN LAST THREE YEARS
  • RECYCLING OF BLEACHING BACK WATER
  • RECYLING OF SHEETING M/C BACK WATER
  • RECIRCULATION OF COOLING WATER
  • RECLAMATION OF PAPER M/C STOCK
  • BACK WATER

71
CHLORINE CONSUMPTION KG/TON
24
72
FUTURE PLANS
73
FUTURE PLANS CONTD.
 
 
74
FUTURE PLANS
CONTD.
SCHEMES WITH AN INVESTMENT OF Rs 125.08 LACS AND
SAVINGS OF Rs 113.59 LACS
75
SCHEMES IN
HAND INSTALLATION OF WASTE FIRED BOILER
2000 LACS INSTALLATION OF BLACK LIQ CLARIFIER
120 LACS RETROFITTING OF LIME KILN
374 LACS AUTOMATION OF PULP
MILLS BY DCS 300 LACS
76
  • AWARDS RECOGNITIONS
  • SELECTED AS A MODEL UNIT BY CPCB/NPC FOR
  • WASTE MINIMIZATION
  • AWARDED CERTIFICATE OF APPRECIATION
  • FOR ADOPTING CLEANER PRODUCTION
  • TECHNOLOGY UNDER UNEP
  • ECO MARK FOR BAGASSE BASE PAPER BY
  • BUREAU OF INDIAN STANDARDS
  • GREENTECH INDO GERMAN AWARD FOR
  • ENVIRONMENTAL EXCELLENCE 2002
  • BEST ENERGY CONSERVATION AWARD BY
  • INDIAN PAPER MANUFACTURERS
  • ASSOCIATION 2003 AND 2004
  • AWARDED ENERGY EFFICIENT UNIT FOR 2004 BY CII
  • AWARDED FIRST PRIZE FOR ENERGY CONSERVATION
  • FOR 2004 BY MINISTRY OF POWER

77
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