DEMINERALISATION PLANTPRESENTATION ON

MGFACFLBCDEGASSERTOWERWBASBAMBDM PLANT FLOW DIAGRAMG.C.TANK-1G.C.TANK-11DM WATER.TANKDM WATER CONDENSATES FROM 1.All Paper Machines 2.New Fiber line 3.P.D.Plant 4.Coating Plant 5.Turbines etc.Fresh water6.Evaporator-3 300 m3 110 m3100 m3MGF: Multi gravel filter.ACF: Activated carbon filter.LBC : Layered bed cation.WBA: Weak base anion.SBA : Strong base anion.MB : Mixed bed.

IMPORTANCE OF DIFFERENT UNITS MGF : Contains gravels with different grade of pebbles. It will remove suspended matter (TOTAL SUPENDED SOLIDS).

ACF : Contains Activated Carbons AC is defined as highly porous,carbonaceous material.The very large porosity provides a large surface area,which results in exceptional adsorptive properties.Works: Adsorbs Organic load & Chlorine.

LBC: This is having Strong and Weak Cation resins. ( Indion-525 H= 2740 Lts and Indion-236 H=4160 Lts).Here flow of water is from top to bottom and flow of regenerant is from bottom to top.It absorbs hardness : Na,Ca & Mg.These are exchanged with Hydrogen on the resin. In regeneration : Na,Ca & Mg ions. are replaced by Hydrogen ions Reactions: RESINS- H + ions + Water CaCl2,MgSo4,NaCl RESINS-Ca +HCl , H2So4

+HCl RESINS- H + ions+CaCl2,CaSo4 (Drained during regeneration )

DEGASSER: Here Carbon dioxide is removed. Reactions: Carbonic Acid + Air by blower Carbon dioxide + WaterWBA : It is having weak anion resin.(Indion-850 Resin = 2350 Lts) It will absorb all the Free mineral acidity in cation treated water. FMA: Conversation of neutral salt (Chloride,Sulphate & Nitrate ) to their respective mineral acids. EMA: Equivalent mineral Acidity a measure of the neutral salts (Chloride,Sulphate & Nitrate ) content of the water. EMA-FMA = Sodium Slip

SBA: This is having Strong anion resins. ( Indion-FFIP = 5690 Lts).Here flow of water is from top to bottom and flow of regenerant is from bottom to top. It absorbs : Chloride,Sulphate,Nitrate and Silica Reactions: RESINS- OH - ions + HCl,H2So4,

RESINS-Cl, So4 + H2O

+NaOH RESINS- OH - ions+ NaCl,Na2So4 (Drained during regeneration )

MB: This the final polishing unit. It contains both cation and anion resins ( Indion-FFIP=1210 Lts and Indion-225 H=2360 Lts) . If there is some traces of hardness and anions leakages,then these are absorbs in MB. Cation resins : are regenerated with HCl. Anion resins : are regenerated with NaOH.DM Water Parameters1.pH = 6.8 to 7.22.Conductivity = 0.5 PPM ( Max)3.Silica = 0.02 PPM ( Max)4.Total Hardness = NiL

Boiler water parameters1.pH = 8.7 to 9.52.Silica = 5 PPM (Max)3.Total Dissolved Solid = 50 PPM(Max)4.Total Hardness = NILSteam 1.pH = 8.5 to 9.02.Silica = 0.02 PPM (Max)3.Total Dissolved Solid = 8 Micro Simens/Cm(Max)4.Total Hardness = NIL

Return Condensate1.pH = 8.5 to 9.02.Silica = 0.02 PPM (Max)3.Conductivity = 8 PPM(Max)4.Total Hardness = NIL

Return Condensate received at G.C.TankAll Paper Machines ( 5 Nos)PD PlantCoating PlantFiber LineTG Sets ( 3 Nos)Evaporators ( 2 Nos)Condensate from LFB-4CFB-5 Feed Water Heater

CONDENSATE BALANCETotal Feed water =DM Water ( Make up) + Return Condensate.Make Up Water = 30 % Return Condensate = 70 % Steam Generated = 4051 M3/Day Expected Condensate = 3195 M3/Day ( 68.28 % ) Actual Condensate received = 2888 M3/Day ( 82.40 % ) Deviation of Condensate = 307 M3/Day ( 14.13 % ) Make up Water = 1276 M3/Day ( 31.41% ) Total CBD/IBD = 41 M3/Day Total Feed Water = 4092 M3/Day

FF-MM

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

DAILY RETURN CONDENSATE BALANCE

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

LPMPHPTOTALNON RECOVRABLERECOVARABLEEXPECTEDACTUALDEVIATION

MTMTMTMTMTMT%M3%M3%M3

1PAPER MACHINES

AP M/C I33300333303038628883275413Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II0620622599156895521Dandy shower 4%

CP M/C III23600236223494222831951127Dandy shower 1%

DP M/C IV148001484144921379113512Dandy shower 3%

EP M/C V1750017525151821437913835Dandy shower 2%,starch prep.12%

TOTAL M/C893620954648918984684798548

2PD PLANT36003603695347025259

3COATING PLANT0

AHEAT EXCHANGER065065065956270452516Exhaust vent loss 1%

BDRYERS CYLINDERS20002002095197014255

CSUPER CALENDER1200120129511708253

COATING PLANT TOTAL3265097097959270682524

4PULP MILL0

ARDH03780378037895359702652595

BFIBRE LINE213002132130000Warm water tank,Bleaching.

CCHLORINE GASSIFIER3900390399537009537

DClO2 PLANT30003022723700237Chiller

P/MILL TOTAL2813780659235424614034026521138

5S.R. PLANT0

ACAUSTICIZING0

a) MAKING HOT WATER3600363600001.52 T/Hr steam is used

b) GREEN LIQUOR HEATING49004904995460095462 T/Hr steam is used

c) FORMAINTAINING CAUSTICIZER TEMP2600262600001.08 T/Hr steam is used

d) SPOUT USE1000101000000.4 T/Hr steam is used

CAUSTICIZING TOTAL1210012173493846003846

BEVAPORATOR-I0

a) FIRST BODY000000000000

b) PRE-HEATER000000000000Ejector running 21 Hr @ 1T/Hr Steam used

c) STEAM JET EJECTOR000000000000

EVAPORATOR-I TOTAL000000000000

CEVAPORATOR-III0

a) FINISHER BODY50700507050795481814101471

b) STEAM JET EJECTOR090990000Ejector running 263 Hr @ 1T/Hr Steam used

EVAPORATOR-III TOTAL5079051695079348185439842

DLFB 40

a) DEAERATOR60006006095579557002.5 T/Hr Steam is used

b) B/L HEATER0909900.37T/Hr Steam is used

c) AIR HEATER57238008095769576003.33 T/Hr Steam is used

d) SMELT SHATTERING0707700000.27 T/Hr Steam is used

e) CASCADE FOR B/L HEATING0110111100000.46 T/Hr Steam is used

f) SOOT BLOWER0022222200000.926 T /Hr Steam is used

g) OIL HEATING & TRACING01101101195119511000.46 T/Hr Steam is used

h) LINE FLUSHING0220222200000.92 T/Hr Steam is used

LFB 4 TOTAL65132262227115165144651440

ELFB 50

a) DEAERATOR66006606695629562002.6 T/Hr Steam used

b) B/L HEATER070725494494000.3 T/Hr Steam used

c) AIR HEATER4633710719568956800LP=0.18 T/Hr,MP=2.64 T/Hr & HP=0.139 T/Hr Steam used

d) SMELT SHATTERING0505500000.197 T/Hr Steam is used

e) SOOT BLOWER00241241242170001 T/Hr Steam is used

f) OIL HEATING & TRACING0505500000.197 T/Hr Steam is used

g) LINE FLUSHING0505500000.197 T/Hr Steam is used

LFB 5 TOTAL708524439940358331333313300

6CFB INTERNAL0

a) CFB-5 FEED WATER HEATER72007207295699569003 T/Hr Steam is used

b) DEAERATORS25700257025795244952440010.69 T/Hr Steam is used

7TURBINE00703703070310070310070300

8CBD004141041000

9STEAM BLOW001515150000

GRAND TOTAL FEED WATER23347301050409250735857831957128878308

Water used for Steam Generation ( 4092 M3 ) = Steam Generated ( 4051 M3) + CBD Losses ( 41 M3)

Total Steam Generation = 4051 M3/Day

Total Feed water =4092 M3/Day

Total Expected Condensate =3195 M3/Day ( 78 %)

Actual Condensate received = 2887 M3/Day ( 71 %)

Condensate to be recovered ( Deviation) = 308 M3/Day ( 8 %)

Gen Manager (Power Block)

Sheet6

NOV-05

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR THE MONTH OF NOV-05

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

LPMPHPTOTALNON RECOVRABLERECOVARABLEEXPECTEDACTUALDEVIATION

MTMTMTMTMTMT%M3%M3%M3

1PAPER MACHINES

AP M/C I9994009994900909486.4863969.16907171732Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II018580185874178491.2169570.8131520380Dandy shower 4%

CP M/C III707700707771700694.0665670.85012231644Dandy shower 1%

DP M/C IV4449004449134431592.1409979.2352213577Dandy shower 3%

EP M/C V5255005255736451981.7429369.8367012623Dandy shower 2%,starch prep.12%

TOTAL M/C26775185802863319152671888.6253827120426174956

2PD PLANT10750010750107595.010217075325269

3COATING PLANT0

AHEAT EXCHANGER01946019460194695.0184970.0136225487Exhaust vent loss 1%

BDRYERS CYLINDERS60100601060195.057170.042125150

CSUPER CALENDER35000350035095.033370.02452588

COATING PLANT TOTAL9511946028970289795.0275270202825724

4PULP MILL0

ARDH01134601134601134695.01077970.07942252837

BFIBRE LINE6384006384638400.00.00Warm water tank,Bleaching.

CCHLORINE GASSIFIER11600011600116095.011020.00951102

DClO2 PLANT8900089067421623.12050.0023205Chiller

P/MILL TOTAL84341134601978070581272261.112086407942214144

5S.R. PLANT0

ACAUSTICIZING0

a) MAKING HOT WATER1092001092109200.00.001.52 T/Hr steam is used

b) GREEN LIQUOR HEATING14550014550145595.013820.009513822 T/Hr steam is used

c) FORMAINTAINING CAUSTICIZER TEMP7820078278200.00.001.08 T/Hr steam is used

d) SPOUT USE3120031231200.00.000.4 T/Hr steam is used

CAUSTICIZING TOTAL36410036412186145538.013820.00381382

BEVAPORATOR-I0

a) FIRST BODY87008708795.0830.009583

b) PRE-HEATER22002202295.0210.009521Ejector running 21 Hr @ 1T/Hr Steam used

c) STEAM JET EJECTOR0210212100.00.00

EVAPORATOR-I TOTAL1092101302110979.71040.0080104

CEVAPORATOR-III0

a) FINISHER BODY15205001520501520595.01444572.511018233427

b) STEAM JET EJECTOR0263026326300.00.00Ejector running 263 Hr @ 1T/Hr Steam used

EVAPORATOR-III TOTAL152052630154682631520593.4144457111018223427

DLFB 40

a) DEAERATOR18000018000180095.0171095.01710002.5 T/Hr Steam is used

b) B/L HEATER0267026726700.37T/Hr Steam is used

c) AIR HEATER150215010024000240095.0228095.02280003.33 T/Hr Steam is used

d) SMELT SHATTERING0199019919900.00.000.27 T/Hr Steam is used

e) CASCADE FOR B/L HEATING0333033333300.00.000.46 T/Hr Steam is used

f) SOOT BLOWER0066766766700.00.000.926 T /Hr Steam is used

g) OIL HEATING & TRACING03330333033394.931694.9316000.46 T/Hr Steam is used

h) LINE FLUSHING0667066766700.00.000.92 T/Hr Steam is used

LFB 4 TOTAL1950394976766662133453364.643066543060

ELFB 50

a) DEAERATOR19680019680196895.0187095.01870002.6 T/Hr Steam used

b) B/L HEATER021902196515449.210849.2108000.3 T/Hr Steam used

c) AIR HEATER132190010021320213295.0202595.0202500LP=0.18 T/Hr,MP=2.64 T/Hr & HP=0.139 T/Hr Steam used

d) SMELT SHATTERING0142014214200.00.000.197 T/Hr Steam is used

e) SOOT BLOWER0072272272200.00.001 T/Hr Steam is used

f) OIL HEATING & TRACING0142014214200.00.000.197 T/Hr Steam is used

g) LINE FLUSHING0142014214200.00.000.197 T/Hr Steam is used

LFB 5 TOTAL2100254582254671213425473.2400373400300

6CFB INTERNAL0

a) CFB-5 FEED WATER HEATER21730021730217395.0206495.02064003 T/Hr Steam is used

b) DEAERATORS77030077030770395.0731895.073180010.69 T/Hr Steam is used

7TURBINE00211002110002110010021100100.02110000

8CBD0012191219012190.00.00

9STEAM BLOW0017717717700.00.00

GRAND TOTAL FEED WATER70116219072410611612914966101163839596370809581315005

Water used for Steam Generation ( 116129 M3 ) = Steam Generated ( 114910 M3) + CBD Losses ( 1219 M3)

705

Total DM Water Make up = 38171 M3

DM Water Supplied to ClO2 Plant = 150 M3

DM Water Supplied to Boiler for Hydraulic use = 650 M3

DM Water Supplied to Vedanta Alumina = 200 M3

Total DM Water extra used = 1000 M3

DM Water used for regeneration =2000 M3

Actual DM Water Make up = 35171 M3

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

Sheet7

J.K. PAPER MILLS : JAYKAPUR

POWER BLOCK

RETURN CONDENSATE BALANCE IN M3 FOR THE MONTH OF APRIL - 03

SUB SOIL WELL

WATER

120800

978177931597157893

RIVER37093

NAGAVALI931597

46580TO MILLSEffluent

894504

DESLUDGING134209

LOSSESBore Well Water

25719

RC408519276822303350000340015704

7210342000239874116032899038148272007461

5500

111840851

1118

+5500C.T. of Evp-3

3992441160

551788130

52442222693

Process: 28455m3 / day

D.M. Plant:1362m3 / day316630457783230708813348

Domestic: 5263m3 / day2186127360684047500

Recycled water used in Pulp Mill 10966 m3 / day

Recycled water used in Evp.- III cooling tower (from compressor) 1372 m3 / day

Recycled water used in Chipper 960 m3 / day

Bore Well Water is used in Pulp Mill as 857 m3/Day

R.C =Return condensate 2403m3 / day

Others: Amn,gardening,toilets, canteen

WATER IN TAKE

CLARIFIER

RESERVOIR

DOMESTIC PURPOSE

POWER BOILER

DM PLANT

COMPRESSOR HOUSE

PB COOLING TOWER

RECOVERY BOILER

PULP MILL + CHIPPER

P.D. PLANT

PAPER MACHINES

OTHERS

WATER RECLAMATION PLANT

EFFLUENT TREATMENT PLANT 837616

COOLING TOWER

COOLING TOWER

Sheet1

LOSS DUE TO POOR(OLD) INSULATION

POWER BLOCK

AVE.AMB.TEMP. 28DATE 17 01 2002

AVE.EXP.TEMP.AFT.INS. 38

SL.NOLOCATIONAREA (APPOX)AVE.SKIN TEMP.PRESENT EXTRA TEMP.MONEY LOSS/DAYCOST OF INS.PAY BACK

12.5 MWTG

H P HEADER20592114000

2M P HEADER256931

3L P HEADER306224

5.4MWTG

4H P HEADER205517

6CFB 1&2

H P LINE1005618

7CFB-4 HP LINE

AFTER R/V707638

8CFB-1&2

STEAM DRUM306729

9CFB 2&5

ESP90

10TOTAL405

ENERGY LOSS =114 W / 0C / M2 ( REF M/S JNM DATA BOOK PAGE 1&6 )GCV OF COAL = 4000 k cal / kg

=114 X 1 cal/s/0c/m2Boiler Efficiency = 85 %

4.18Cost of coal = Rs 950 /-per ton

=114 X 60 X 60 X24kcal / day / 0c / m2savingEnergy loss x Cost of coal x Extra temp

4.18 X 1000GCV of Coal x boiler efficency

=2356kcal / day / 0c / m2

steam

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCK

STEAM BALANCING INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTION

(ON DAY AVE.FOR THE MONTH OFJULY 2000)

BASESI.NODESCRIPTIONPRODUCTIONSTEAM MTACTUALTARGETREMARKS

MTHPMPLPEQV.HPT/TT/T

PAPER MACHINE -- I973262902.992.94

-- II14.479714.884.82

-- III92.973092752.963

-- IV28.45108963.383.3

-- V55.581911703.062.97

1TOTAL288.45799349023.133.1

PD2PD PLANT (AD)13.8751453.273.13

RDH4413921.451.34

PULPFIBER LINE2382120.780.8

GASSIFIER36320.120.13

CLO2 PLANT57510.190.26

3TOTAL2714413316872.542.53

PULPEVAPORATOR4724201.551.4

C.S PLANT1191060.390.38

LF BOILER IV4060601470.540.59

LF BOILER V6091912220.820.7

4TOTAL2711001517428953.33.07

5CF BOILER'S INTERNAL USE288.452522240.780.74

6STEAM BLOW OUT ,RADIATION288.4552520.180.18Steam blow =2 T Rest losses

PAPERAND TRAP LOSS.

7STEAM TO TURBINE288.457614726410383.63.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER288.458134751613144.564.2Steam for PH +CFB Int+Losses (5+6+7)

BOILERS.

9TOTAL STEAM288.459137182574384313.3212.19

PULP10STEAM FOR PULP(3+4)271100592107315825.845.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)42.392235.845.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD)50.65341Steam for salable pulp + steam for PD sheet

(SCREW PULP+PD SHEET)0.9

13PULP FOR PAPER(1-13)220.3512875.845.6Total Pulp - Salable Pulp,i.e(10-12)

PAPER14PROCESS STEAM FOR PAPER288.4521887.67.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE.

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89

( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89

( MEASURED BEFORE INJECTION )Gen. Manager (Power Block)

J.K PAPER MILLS,JAYKAY PURJ.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR APRIL -- 2001Date: 01.05.2001FOR APRIL -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATIONBASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/TMTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I29342934112801128010039100393.423.422.94This MonthTodateThis MonthTodatePAPER MACHINE I000.000.002.94This MonthTodateThis MonthTodate

II43243218751875166916693.863.864.82CFB 1155311553112 MWTG72238007223800II000.000.004.82CFB 112 MWTG

III2546254673577357654865482.572.573CFB 210422104225.4 MWTG34862903486290III000.000.003CFB 25.4 MWTG

IV1051105142864286381538153.633.633.3CFB 3300030002.5 MWTG15330001533000IV000.000.003.3CFB 32.5 MWTG

V1740174049054905436543652.512.512.97CFB 41234612346TOTAL.1224309012243090V000.000.002.97CFB 4TOTAL.

1TOTAL8703870318751875278282782826436264363.043.043.1CFB 53890038900STEAM1TOTAL000.000.003.1CFB 5STEAM

PD2PD PLANT (AD)1042104222262226198119811.901.903.13Sub Total.8019980199EXTR - 12670026700PD2PD PLANT (AD)000.000.003.13Sub Total.EXTR - 1

RDH76527652131501315011704117041.531.531.34LFB 41663416634EXTR - 26499964999RDH000.000.001.34LFB 4EXTR - 2

PULPFIBER LINE7652765272377237644164410.840.840.8LFB 52262422624Condensate2631026310PULPFIBER LINE000.000.000.8LFB 5Condensate

GASSIFIER7652765211631163103510350.140.140.13Grand Total119457119457PRDS14481448GASSIFIER000.000.000.13Grand TotalPRDS00

CLO2 PLANT765276529189188178170.110.110.26Coal1686216862Tot.Equ Coal1794717947CLO2 PLANT000.000.000.26CoalTot.Equ Coal

3TOTAL7652765213150131509318931819997199972.612.612.53B.Dust656656Steam / Kg of coal4.4694.4693TOTAL000.000.002.53B.DustSteam / Kg of coal0.0000.000

PULPEVAPORATOR76527652134941349412010120101.571.571.4Charcoal fines636636PULPEVAPORATOR000.000.001.4Charcoal fines

CAUSTICIZING Plant7652765237133713330533050.430.430.38REMARKSCAUSTICIZING Plant000.000.000.38REMARKS

LF BOILER IV76527652120012001823182318231823444544450.580.580.5940TPD FOR S/B,REST 50%MP,50%LPLF BOILER IV000.000.000.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V76527652180018003145314520962096646464640.840.840.760TPD FOR S/B ,REST 60% MP,40%LPLF BOILER V000.000.000.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL765276523000300049684968211262112626224262243.433.433.074TOTAL000.000.003.07

5CF Boiler's internal8703870384938493755975590.870.870.745CF Boiler's internal000.000.000.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES87038703339333930.390.390.181163 Tons by Steam Blow and rest by losses.6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES000.000.000.181163 Tons by Steam Blow and rest by losses.

PAPERPAPER

7STEAM TO TURBINE870387032631026310142714277065706533868338683.893.893.28Condensate +equivalent enrgy drop in extractions7STEAM TO TURBINE000.000.003.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS8703870344820448205.155.154.2Steam for PH +CFB Int+Losses (5+6+7)8STEAM TO TURBINES & POWER BOILERS000.000.004.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM8703870311945711945713.7313.7312.199TOTAL STEAM000.000.0012.19

PULP10Steam for Pulp(3+4)7652765246220462206.046.045.6Steam consumed in Pulp Mill & RecoveryPULP10Steam for Pulp(3+4)000.000.005.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)52523143146.046.045.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP11SCREW PULP (AD)000.000.005.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,9985985792879288.058.05Steam for salable pulp + steam for PD sheet12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,9000.000.00Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)6667666738292382925.745.745.6Total Pulp - Salable Pulp,i.e(10-12)13Pulp for Paper(10-12)000.000.005.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper8703870366709667097.677.677.25(9-8-12)Paper14Process Stream for Paper000.000.007.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BESTNOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/KgKg/CM2DEG.CK.cal/Kg

HP STEAM354107751HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

Gen. Manager (Power Block)Gen. Manager (Power Block)

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR JUNE -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I30828719113683282310118292123.283.352.94This MonthTodateThis MonthTodate

II440133718305527162949193.703.684.82CFB 1172465011812 MWTG725460021356800

III260679577429226076612201202.542.533CFB 216999449725.4 MWTG360576010678550

IV98831294134130203679115883.723.703.3CFB 3045292.5 MWTG15804004683760

V182553985014150894462134292.452.492.97CFB 4143520718TOTAL.1244076036719110

1TOTAL89412654018305527279458353926500792692.962.993.1CFB 541713116437STEAM

PD2PD PLANT (AD)1431357329007501258166761.801.873.13Sub Total.77393236774EXTR - 12688580856

RDH798023492125743863011191343811.401.461.34LFB 41750551022EXTR - 266010194530

PULPFIBER LINE7980234927847212516984189130.880.810.8LFB 52565570327Condensate2724280122

GASSIFIER79802349211703542104131520.130.130.13Grand Total120553358123PRDS4162615

CLO2 PLANT798023492900273480124330.100.100.26Coal1642149394Tot.Equ Coal1685751926

3TOTAL798023492125743863099172752720017588802.512.512.53B.Dust6402000Steam / Kg of coal4.5914.560

PULPEVAPORATOR798023492128123985411403354701.431.511.4Charcoal fines01176

CAUSTICIZING Plant7980234924239119933773106740.470.450.38REMARKS

LF BOILER IV7980234921200336017493572174954204313113630.540.480.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V7980234921800510033416486222762256756164130.850.700.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL79802349230008460509010058210276349226244739203.293.153.07

5CF Boiler's internal8941265408267252427358224650.820.850.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES8941265402975144480.330.540.18761 Tons by Steam Blow and rest by losses.

PAPER

7STEAM TO TURBINE894126540272428012210784049750221056348781024653.903.863.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS894126540452111393795.065.254.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM89412654012055335812313.4813.4912.19

PULP10Steam for Pulp(3+4)798023492462611327995.805.655.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)011806675.805.655.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,91288332210047254547.807.66Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)669220170362141073455.415.325.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper894126540652951932897.307.287.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

Gen. Manager (Power Block)

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR JULY -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I29821170110604434279438386503.163.302.94This MonthTodateThis MonthTodate

II396173316177144143963583.633.674.82CFB 1176506776812 MWTG736750028724300

III2490104476920295276159262792.472.523CFB 217879628515.4 MWTG335892014037470

IV105641854325173453849154373.653.693.3CFB 3045292.5 MWTG16008766284636

V171571134931200204389178182.562.502.97CFB 4288823606TOTAL.1232729649046406

1TOTAL8639351791617714426780110319252731045422.932.973.1CFB 542651159088STEAM

PD2PD PLANT (AD)12874860281310314250491791.951.893.13Sub Total.81068317842EXTR - 124801105657

RDH770131193115115014110245446251.331.431.34LFB 41427365295EXTR - 267684262214

PULPFIBER LINE7701311937416286676600255140.860.820.8LFB 52596896295Condensate28501108623

GASSIFIER77013119311904732105942110.140.140.13Grand Total121309479432PRDS3232938

CLO2 PLANT770131193922365682132540.110.100.26Coal1796867362Tot.Equ Coal1801369939

3TOTAL770131193115115014195283705518725776042.432.492.53B.Dust662066Steam / Kg of coal4.5014.545

PULPEVAPORATOR770131193132665312011807472771.531.521.4Charcoal fines01176

CAUSTICIZING Plant7701311934399163923915145890.510.470.38REMARKS

LF BOILER IV7701311931240460013664939136667863671150350.480.480.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V7701311931860696034339919228985146953233650.900.750.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL7701311933100115604799148582132084812263461002663.423.213.07

5CF Boiler's internal8639351799024342668031304970.930.870.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES8639351793228176760.370.500.182316 Tons by Steam Blow and rest by losses.

PAPER

7STEAM TO TURBINE8639351792850110862314925541828429340372021396674.313.973.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS863935179484611878405.615.344.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM86393517912130947943214.0413.6312.19

PULP10Steam for Pulp(3+4)770131193450711778715.855.705.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)011806730.005.705.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,9115844802504347272.167.75Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)654326713425671431446.515.365.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper863935179703442568668.147.307.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

Gen. Manager (Power Block)

N190=L190/D190

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR AUGUST -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I31161481710598540259432480823.033.252.94This MonthTodateThis MonthTodate

II440217317298873153978973.503.634.82CFB 1175928536012 MWTG578690034511200

III2878133257997375247117333962.472.513CFB 218328811795.4 MWTG350424017541710

IV107652614257216023789192263.523.653.3CFB 3335078792.5 MWTG15832007867836

V164087534820248404290221082.622.532.97CFB 4751731123TOTAL.1087434059920746

1TOTAL9150443291729887327672137991261671307092.862.953.1CFB 528157187245STEAM

PD2PD PLANT (AD)167865383533138473144123241.871.883.13Sub Total.74944392786EXTR - 123444129101

RDH850339696113316147210085547101.191.381.34LFB 41761482909EXTR - 260112322326

PULPFIBER LINE8503396966856355236102316150.720.800.8LFB 524417120712Condensate23542132165

GASSIFIER85033969611805912105052620.120.130.13Grand Total116975596407PRDS987712815

CLO2 PLANT850339696910456681040640.100.100.26Coal1679084152Tot.Equ Coal1679086729

3TOTAL850339696113316147289464600118047956512.122.412.53B.Dust02066Steam / Kg of coal4.4644.529

PULPEVAPORATOR850339696130326615211598588751.361.481.4Charcoal fines01176

CAUSTICIZING Plant8503396964613210054106186940.480.470.38REMARKS

LF BOILER IV8503396961160576018796818188186674506195420.530.490.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V850339696180087603443133622295108096907302720.810.760.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL85033969629601452053222018021821106633271171273843.193.213.07

5CF Boiler's internal9150443298694429607738382340.850.860.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES9150443293006206810.330.470.181426 Tons by Steam Blow and rest by losses.

PAPER

7STEAM TO TURBINE9150443292354213216514807021775037090317571714243.473.873.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS915044329425002303404.645.204.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM91504432911697559640712.7813.4512.19

PULP10Steam for Pulp(3+4)850339696451642230355.315.625.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)011806630.005.625.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,9151059903144459812.087.68Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)699333706420191770536.015.255.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper915044329713313200867.807.227.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

Gen. Manager (Power Block)

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR SEPTEMBER -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I28811769810230642559105571873.163.232.94This MonthTodateThis MonthTodate

II4302603171610589152794243.553.624.82CFB 11485010021012 MWTG615650040667700

III2362156877030445546257396532.652.533CFB 214848960275.4 MWTG351700021058710

IV95162123903255053474226993.653.653.3CFB 320680852.5 MWTG15225009390336

V1623103764900297404361264692.692.552.97CFB 4379634919TOTAL.1119600071116746

1TOTAL82475257617161058926063164054247231554323.002.963.1CFB 539274226519STEAM

PD2PD PLANT (AD)180183394077179243629159522.011.913.13Sub Total.72974465760EXTR - 125638154739

RDH816047856119447341610630653401.301.371.34LFB 418185101094EXTR - 259618381944

PULPFIBER LINE8160478567126426496342379580.780.790.8LFB 522727143439Condensate22451154616

GASSIFIER81604785611607072103262940.130.130.13Grand Total113886710293PRDS617918994

CLO2 PLANT816047856898546479948630.100.100.26Coal1554199693Tot.Equ Coal15955102684

3TOTAL8160478561194473416918455185188041144552.302.392.53B.Dust6162682Steam / Kg of coal4.5744.536

PULPEVAPORATOR816047856130557920711619704941.421.471.4Charcoal fines01176

CAUSTICIZING Plant8160478564410254153925226190.480.470.38REMARKS

LF BOILER IV81604785611206880191887361917105844533240750.560.500.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V8160478561680104403188165502126129356409366820.790.770.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL81604785628001732051062528621508128141264861538703.253.223.07

5CF Boiler's internal8247525768589515497644458790.930.870.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES8247525762336230180.280.440.18448 Tons by Steam Blow and rest by losses.

PAPER

7STEAM TO TURBINE8247525762245115461612818302749744587302632016873.673.843.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS824752576402442705834.885.154.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM82475257611388671029313.8113.5112.19

PULP10Steam for Pulp(3+4)816047856452902683255.555.615.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)011806620.005.615.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,9162176113629586282.247.70Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)653940245416622096976.375.215.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper824752576700143810818.497.257.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

Gen. Manager (Power Block)

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR OCTOBER -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I2589202879963742188867660543.423.262.94This MonthTodateThis MonthTodate

II40130041674122631490109143.723.634.82CFB 11451511472512 MWTG438410045051800

III2746184337882524367015466682.552.533CFB 2128121088395.4 MWTG368288024741590

IV109973114377298823896265953.543.643.3CFB 3080852.5 MWTG146800910858345

V1756121325160349004592310612.622.562.97CFB 472435643TOTAL.953498980651735

1TOTAL85916116716741226327382191436258601812923.012.963.1CFB 540012266531STEAM

PD2PD PLANT (AD)151998583416213403040189932.001.933.13Sub Total.68063533823EXTR - 119503174242

RDH758255438120138542910692760321.411.371.34LFB 416964118058EXTR - 255633437577

PULPFIBER LINE7582554386064487135397433550.710.780.8LFB 523957167396Condensate18495173111

GASSIFIER75825543812038275107173650.140.130.13Grand Total108984819277PRDS1535334347

CLO2 PLANT758255438884634878756500.100.100.26Coal14524114217Tot.Equ Coal14943117627

3TOTAL7582554381201385429815163336179461324012.372.392.53B.Dust6333315Steam / Kg of coal4.5554.538

PULPEVAPORATOR758255438123769158311015815091.451.471.4Charcoal fines01176

CAUSTICIZING Plant7582554384697301124180268000.550.480.38REMARKS

LF BOILER IV758255438114080201838105741839124234413284870.580.510.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V7582554381740121803311198612207151426651433330.880.780.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL75825543828802020051493043521119149260262591801293.463.253.07

5CF Boiler's internal8591611677873594227007528860.820.860.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES8591611672833258510.330.420.18840 Tons by Steam Blow and rest by losses.

PAPER

7STEAM TO TURBINE8591611671849517311112519553722651813260402277273.033.723.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS859161167358793064634.185.014.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM85916116710898481927712.6913.3912.19

PULP10Steam for Pulp(3+4)758255438442043125295.835.645.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)011806650.005.645.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,9136789783040696082.227.75Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)621546460411642429216.625.235.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper859161167700644432068.167.257.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

Gen. Manager (Power Block)

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR NOVEMBER -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I29562324310472846909320753743.153.242.94This MonthTodateThis MonthTodate

II42534291668139311485123993.493.624.82CFB 11453912926412 MWTG623640051288200

III2671211047737601736886535542.582.543CFB 2135861224255.4 MWTG310392027845510

IV89582063777336593362299573.763.653.3CFB 3080852.5 MWTG141580012274145

V1672138045213401134640357012.772.592.97CFB 4163437277TOTAL.1075612091407855

1TOTAL86196978616681393127199218635256922069842.982.973.1CFB 540604307135STEAM

PD2PD PLANT (AD)1680115383717250573308223011.971.933.13Sub Total.70363604186EXTR - 119185193427

RDH810263540117409716910449864801.291.361.34LFB 417362135420EXTR - 269816507393

PULPFIBER LINE8102635406185548985505488590.680.770.8LFB 523773191169Condensate20836193947

GASSIFIER81026354011509425102483880.130.130.13Grand Total111498930775PRDS166136008

CLO2 PLANT810263540880722878364330.100.100.26Coal14768128985Tot.Equ Coal15307132934

3TOTAL8102635401174097169821571551177601501612.192.362.53B.Dust7954110Steam / Kg of coal4.5974.545

PULPEVAPORATOR8102635401224110382410894924031.341.451.4Charcoal fines01176

CAUSTICIZING Plant8102635405076351884518313170.560.490.38REMARKS

LF BOILER IV810263540120092201861124351862142854513330010.560.520.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V8102635401800139803153230142102172446477498100.800.780.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL81026354030002320050143544921281170541264032065313.263.253.07

5CF Boiler's internal8619697868465678877534604190.870.870.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES8619697861896277470.220.400.18362 Tons by Steam Blow and rest by losses.

PAPER

7STEAM TO TURBINE86196978620836193947105810611800959822289062566323.353.683.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS861969786383363447994.454.944.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM86196978611149893077512.9413.3412.19

PULP10Steam for Pulp(3+4)810263540441633566925.455.615.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)011806620.005.615.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,91512104909157811906.067.74Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)659053050350052755025.315.195.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper861969786640055047867.437.237.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

Gen. Manager (Power Block)

J.K PAPER MILLS,JAYKAY PUR

POWER BLOCKQF / 030 / 55

STEAM DISTRIBUTION INTERMS OF EQUIVALENT HP STEAM / TON OF MACHINE PRODUCTIONRev. No. 001

FOR DECEMBER -- 2001Date: 01.05.2001

BASESI.NODESCRIPTIONProductionSTEAM MTACTUALTARGETSTEAM & POWER GENERATION

MTHPMPLPEQV.HPT/TT/T

This MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateThis MonthTodateBOILERTotal Gen.TGTotal Gen.

PAPER MACHINE I2997262400846900753740.002.872.94This MonthTodateThis MonthTodate

II45438830139310123990.003.194.82CFB 1012926412 MWTG051288200

III2878239820601730535540.002.233CFB 201224255.4 MWTG027845510

IV119682060336590299570.003.653.3CFB 3080852.5 MWTG012274145

V1702155060401130357010.002.302.97CFB 4037277TOTAL.091407855

1TOTAL922777817013931021863502069840.002.663.1CFB 50307135STEAM

PD2PD PLANT (AD)1263128010250570223010.001.743.13Sub Total.0604186EXTR - 10193427

RDH8201717410971690864800.001.211.34LFB 40135420EXTR - 20507393

PULPFIBER LINE8201717410548980488590.000.680.8LFB 50191169Condensate0193947

GASSIFIER82017174109425083880.000.120.13Grand Total0930775PRDS036008

CLO2 PLANT82017174107228064330.000.090.26Coal0128985Tot.Equ Coal0132934

3TOTAL82017174109716907155101501610.002.092.53B.Dust04110Steam / Kg of coal0.0004.545

PULPEVAPORATOR82017174101038240924030.001.291.4Charcoal fines01176

CAUSTICIZING Plant8201717410351880313170.000.440.38REMARKS

LF BOILER IV820171741092200124350142850330010.000.460.5940TPD FOR S/B,REST 50%MP,50%LP

LF BOILER V8201717410139800230140172440498100.000.690.760TPD FOR S/B ,REST 60% MP,40%LP

4TOTAL820171741023200035449017054102065310.002.883.07

5CF Boiler's internal9227778170678870604190.000.780.74

6STEAM BLOW OUT ,RADIATION AND TRAP LOSSES9227778170277470.000.360.18362 Tons by Steam Blow and rest by losses.

PAPER

7STEAM TO TURBINE922777817019394701061105982202566320.003.303.28Condensate +equivalent enrgy drop in extractions

8STEAM TO TURBINES & POWER BOILERS92277781703447990.004.434.2Steam for PH +CFB Int+Losses (5+6+7)

9TOTAL STEAM92277781709307750.0011.9612.19

PULP10Steam for Pulp(3+4)82017174103566920.004.975.6Steam consumed in Pulp Mill & Recovery

11SCREW PULP (AD)011805870.004.975.6SCREW PULP(AD)*0.9*STEAM/TON OF PULP

12SALABLE PULP (BD) (SCREW PULP+PD SHEET)*0,91137116270801100.006.89Steam for salable pulp + steam for PD sheet

13Pulp for Paper(10-12)70646011402765820.004.605.6Total Pulp - Salable Pulp,i.e(10-12)

Paper14Process Stream for Paper92277781705058660.006.507.25(9-8-12)

NOTE:TARGETS ARE FIXED ON THE BASIS OF MAY 2000 PERFORMANCE WHICH IS BEST

Kg/CM2DEG.CK.cal/Kg

HP STEAM354107751

MP STEAM92206860.89( MEASURED AFTER INJECTION )

LP STEAM2.82106880.89( MEASURED BEFORE INJECTION )

LOSS DUE TO POOR(OLD) INSULATION

Gen. Manager (Power Block)

AVE.AMB.TEMP. 28

AVE.EXP.TEMP.AFT.INS. 38

SL.NOLOCATIONAREA (APPOX)AVE.SKIN TEMP.PRESENT EXTRA TEMP.MONEY LOSS/DAYCOST OF INS.PAY BACK

12.5 MWTG

H P HEADER20592114000

2M P HEADER256931

3L P HEADER306224

5.4MWTG

4H P HEADER205517

5L P HEADER205618

6CFB 1&2

H P LINE1005618

7CFB-4 HP LINE

AFTER R/V707638

8CFB-1&2

STEAM DRUM306729

9CFB 2&5

ESP90

10TOTAL405

&R&F

&L&F&T&D

water

J.K.PAPER MILLS , JAYKAYPUR

POWER BLOCK

WATER BALANCE FOR APRIL TO JULY 2000 AVERAGE PER DAY

BASESI.NOPARTCULARSPRODNACTUALTARGETWATER CONSUMED (M3)RECLAMATIONEFFLUENTLOSSESREMARKS

MTM3/TM3/TFRESHRECYCLEDM3%M3%M3%

PAPER1Total water286135.61130387803473289.56404810.44

2To Colony28617.602050304778952525

3To Mills286118110337502995488.75379611.25

PULP4For Pulp25778.2200989B+9C1+9C3+10E+10F+10G+10I+10J+10K+10L+10M

5For saleable Pulp29992868Salaeable pulp*water per Ton of pulp*

PAPER6For Power2867.862247112557625.6155969.49C2+9C4

7For Paper Machines28637.781080589688312951254259A+10A+10B+10C+10D

8For Process286100.1228635(3)-(5)-(6)

921" Pipe13035

PAPER9APM-11003245269383389121635

PULP9BSR Plant2575561141134865031374534953486M3 Water from EVP CT to Pulp Mill HW Tank

PAPER9CPower Block42292026202632.4251840.25171127.35

PULP9C1DM Plant19821914191449194250401Back wash=250,Return con.1914,make up1732

PAPER9C2Cooling Tower217411255032315597223% CBD=0.7% Circu.,72%Evp.&Wid.=2.2% Circu.

PULP9C3Ash Conditioner112112100coal*0.4*0.5

9C4CBD Losses73731% of steam

1018" Pipe Line20715

10APM-215720598838612365

10BPM-3843120258983374121575

10CPM-429180014948321612905

10DPM-558192015948323012965

10EFiber Line54051149416054958455

10FClo2 Plant60057095305

10GChemical Plant48045695245

10HPD Plant60057095305

10ICompressor House14401411982921411 M3 Water to EVP cooling Tower

10JET Plant48045695245

10KReclimation1440141195295

10LOthers27102575951355

10MChipper96091295485

NOTE:SI No 1 to 8 only fresh water considered.

SI No 9A onwards Fresh water and recycled water considered.

Losses = evaporation, windage,seapage , moiture in products ie. Paper,pulp,slurry etc.

Pm/c 1,2,3,4,5,Clo2,NFL and DM Plant make up are having Flow Meters and rest are assumption.Gen. Manager (Power Block)

J.K.PAPER MILLS , JAYKAYPURFormat No. QF / 030 / WS / 04

POWER BLOCKRev. No. 000

WATER BALANCE FOR THE MONTH OFDate : 1.09.2000

BASESI.NOPARTCULARSPRODNACTUALTARGETWATER CONSUMED (M3)RECLAMATIONEFFLUENTLOSSESREMARKS

MTM3/TM3/TFRESHRECYCLEDM3%M3%M3%

PAPER1Total water

2To Colony

3To Mills

PULP4For Pulp9B+9C1+9C3+10E+10F+10G+10I+10J+10K+10L+10M

5For saleable PulpSalaeable pulp*water per Ton of pulp*

PAPER6For Power9C2+9C4

7For Paper Machines9A+10A+10B+10C+10D

8For Process(3)-(5)-(6)

921" Pipe

PAPER9APM-1

PULP9BSR PlantM3 Water from EVP CT to Pulp Mill HW Tank

PAPER9CPower Block

PULP9C1DM PlantBack wash=250,Return con.1914,make up1732

PAPER9C2Cooling Tower23% CBD=0.7% Circu.,72%Evp.&Wid.=2.2% Circu.

PULP9C3Ash Conditionercoal*0.4*0.5

9C4CBD Losses1% of steam

1018" Pipe Line

10APM-2

10BPM-3

10CPM-4

10DPM-5

10EFiber Line

10FClo2 Plant

10GChemical Plant

10HPD Plant

10ICompressor HouseM3 Water to EVP cooling Tower

10JET Plant

10KReclimation

10LOthers

10MChipper

NOTE:SI No 1 to 8 only fresh water considered.

SI No 9A onwards Fresh water and recycled water considered.

Losses = evaporation, windage,seapage , moiture in products ie. Paper,pulp,slurry etc.

Pm/c 1,2,3,4,5,Clo2,NFL and DM Plant make up are having Flow Meters and rest are assumption.Gen. Manager (Power Block)

Flow Diagram

Date : 19.12.05

J.K. PAPER MILLS : JAYKAPUR

POWER BLOCK

DAILY RETURN CONDENSATE BALANCE IN M3

DM Plant

2888

Regeneration,ClO2,SPRD etcG.C.Tanks4092Boilers for Steam Generation

1204

41

CBD / IBD4051

Steam Supplied954369765912151662132970315

Paper MachinesPD PlantCoating PlantPulp MillCausticizing PlantEvaporators ( I & III)LFB-4&5CFB InternalTurbinesSteam Blow

Return Condensate

%%%%%%%%%

1) Expected84688.6792452833495929540361463848193.217054263627744.605475040331395.1367781155703100

2) Actual7988425706870265400043985.077519379827744.605475040331395.1367781155703100

3) Deviation4859252425138214638.0165289256428000000

RETURN CONDENSATE

2888

Steam Generated = 4051 M3/Day

Expected Condensate = 3195 M3/Day ( 68.28 % )

Actual Condensate received = 2888 M3/Day ( 82.40 % )

Deviation of Condensate = 307 M3/Day ( 14.13 % )

Make up Water = 1276 M3/Day ( 31.41% )

Total CBD/IBD = 41 M3/Day

Total Feed Water = 4092 M3/Day

72

1204

1276

Sheet3

Sheet2

Sheet4

Date : 16.08.03

J.K.PAPER MILLS : JAYKAYPUR

POWER BLOCK

EFFECT OF BLEACH LIQUOR ADDITION IN MILL WATER

Daily about 2400Lts of Bleach liquor is used at water supply.Due to the addition of bleach liquor, the calcium hardness and Total hardness is increased in mill water.Following are the observations .

Date & TimeTotal hardness (ppm)Calcium hardness (ppm)

BeforeAfterDifferenceBeforeAfterDifference

13.08.03

7.30 A.M4449528335

8.00A.M4349627336

8.30A.M4449527.5335.5

9.00A.M4448.54.527325

2.30P.M4348530333

3.30P.M4649330322

4.00P.M4348.55.529345

Average43.8648.714.8628.3632.864.5

After addition of bleach liqour there is a increase of 4.5 ppm of calcium hardness and 4.86 ppm of Total hardness.

Drinking water standard (IS 10500:1991)Desirable limit

1.Total hardness300 ppm

2.Calcium as Ca75 ppm

Both parameters are within the limit.

cond-June-03

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR JULY 02.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I9619866875385744075.06568Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1731691662901496791197Dandy shower 4%

CP M/C III7977807897957502704738Dandy shower 1%

DP M/C IV4818145467395443965.03037Dandy shower 3%

EP M/C V5008701430785366160.02584Dandy shower 2%,starch prep.12%

TOTAL M/C291531861272922453818124

2PD PLANT27220272295258645.01225

3PULP MILL

ARDH1153901153985980833.53870

BFIBRE LINE544754470

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP50185018

BEVAPORATORS11757011757951116968.28021

CLFB 46842

ia) S/B161216120

iib) B/L HEATER155015500

iiic) DEAERATOR176701767951679951679

ivd) AIR HEATER170501705951620951620

ve) LINE FLUSHING2082080

DLFB 57756

ia) S/B186018600

iib) B/L HEATER170517050

iiic) DEAERATOR176701767951679851679

ivd) AIR HEATER180001800951710851710

ve) LINE FLUSHING6246240

TOTAL SRP

5CFB INTERNAL860008600958170958170

6TURBINE214150214151002141510021415

7CBD112501125556556

8STEAM BLOW1471470

GRAND TOTAL11366021923917378443067569

Water used for Steam Generation =Steam Generated + CBD Losses

1136601125113660

Expected Return Condensate =84430 M3

Actual Return Condensate =67569 m359.45%

Actual DM Water Make up =46091 m340.55%

Targeted DM Water Make up =39781 m335%

Pm/c 1 & EVP 3 (not working) are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR AUGUST- 02.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I9557860869785739284.57350Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1709681641901477801313Dandy shower 4%

CP M/C III7136717065956715805654Dandy shower 1%

DP M/C IV4918147477195453280.03817Dandy shower 3%

EP M/C V4904687421785358480.03374Dandy shower 2%,starch prep.12%

TOTAL M/C282241833263912370021508

2PD PLANT30050300595285570.02104

3PULP MILL

ARDH11925011925851013634.34093

BFIBRE LINE575557550

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP51085108

BEVAPORATORS13372013372951270364.38598

CLFB 47344

ia) S/B173617360

iib) B/L HEATER161216120

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING4294290

DLFB 57904

ia) S/B186018600

iib) B/L HEATER170517050

iiic) DEAERATOR204602046951944951944

ivd) AIR HEATER179801798951708951708

ve) LINE FLUSHING4954950

TOTAL SRP

5CFB INTERNAL860508605958175958175

6TURBINE212570212571002125710021257

7CBD115001150557557

8STEAM BLOW3203200

GRAND TOTAL11610822744933648592472833

Water used for Steam Generation =Steam Generated + CBD Losses

1149581150116108

Expected Return Condensate =85924 M3

Actual Return Condensate =72833 m363.07%

Actual DM Water Make up =43275 m336.93%

Targeted DM Water Make up =40638 m335%

Pm/c 1 & EVP 3 (not working) are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR SEPT- 02.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I9584863872185741380.06977Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1904761828901645901645Dandy shower 4%

CP M/C III7684777607957227906864Dandy shower 1%

DP M/C IV4798144465495442190.04189Dandy shower 3%

EP M/C V4554638391685332980.03133Dandy shower 2%,starch prep.12%

TOTAL M/C285241798267262403522808

2PD PLANT22840228495217079.21809

3PULP MILL

ARDH11911011911851012436.84379

BFIBRE LINE565256520

CCHLORINE GASSIFIER117011700

DClO2 PLANT900660240

P/MILL TOTAL

4S.R. PLANT

ACSP45474547

BEVAPORATORS12614012614951198372.99190

CLFB 47372

ia) S/B173617360

iib) B/L HEATER161216120

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING4574570

DLFB 57590

ia) S/B186018600

iib) B/L HEATER170517050

iiic) DEAERATOR176701767951679951679

ivd) AIR HEATER180001800951710951710

ve) LINE FLUSHING4584580

TOTAL SRP

5CFB INTERNAL752407524957148957148

6TURBINE152830152831001528310015283

7CBD105701057553553

8STEAM BLOW3543540

GRAND TOTAL10678222009847737757467448

Water used for Steam Generation =Steam Generated + CBD Losses

1057251057106782

Expected Return Condensate =77574 M3

Actual Return Condensate =67448 m363.16%

Actual DM Water Make up =39334 m336.84%

Targeted DM Water Make up =37374 m335%

Pm/c 1 & EVP 3 (not working) are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR NOV- 02.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8542769777385660483.46484Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II2060821978901780801582Dandy shower 4%

CP M/C III7038706968956620805574Dandy shower 1%

DP M/C IV4942148479495455480.03835Dandy shower 3%

EP M/C V4499630386985328980.03095Dandy shower 2%,starch prep.12%

TOTAL M/C270811699253822284720570

2PD PLANT25720257295244380.02058

3PULP MILL

ARDH11957011957851016349.35897

BFIBRE LINE623562350

CCHLORINE GASSIFIER115311530

DClO2 PLANT890650240

P/MILL TOTAL

4S.R. PLANT

ACSP47704770

BEVAPORATORS12912012912951226668.48828

CLFB 47432

ia) S/B186018600

iib) B/L HEATER180018000

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING2052050

DLFB 57630

ia) S/B186018600

iib) B/L HEATER170517050

iiic) DEAERATOR176701767951679951679

ivd) AIR HEATER180001800951710951710

ve) LINE FLUSHING4984980

TOTAL SRP

5CFB INTERNAL882608826958385958385

6TURBINE191020191021001910210019102

7CBD111001110556556

8STEAM BLOW4074070

GRAND TOTAL11207722842892358204063.9571674

Water used for Steam Generation =Steam Generated + CBD Losses

1109671110112077

Expected Return Condensate =82040 M3

Actual Return Condensate =71674 m363.95%

Actual DM Water Make up =40403 m336.05%

Targeted DM Water Make up =39227 m335%

Pm/c 1 & EVP 3 (not working) are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR DEC- 02.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8882799808385687076.86204Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1991801911901720801529Dandy shower 4%

CP M/C III7676777599957219806079Dandy shower 1%

DP M/C IV5107153495495470680.03963Dandy shower 3%

EP M/C V4799672412785350880.03302Dandy shower 2%,starch prep.12%

TOTAL M/C284551781266742402321077

2PD PLANT26300263095249865.01710

3PULP MILL

ARDH12498012498851062355.56930

BFIBRE LINE664966490

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP47104710

BEVAPORATORS12922012922951227670.99158

CLFB 47444

ia) S/B186018600

iib) B/L HEATER180018000

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING2172170

DLFB 58040

ia) S/B200020000

iib) B/L HEATER180018000

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING6736730

TOTAL SRP

5CFB INTERNAL893308933958486958486

6TURBINE203220203221002032210020322

7CBD115001150558558

8STEAM BLOW2462460

GRAND TOTAL11613823627925118506464.1674519

Water used for Steam Generation =Steam Generated + CBD Losses

1161381149881150

Expected Return Condensate =85064 M3

Actual Return Condensate =74519 m364.16%

Actual DM Water Make up =41619 m335.84%

Targeted DM Water Make up =40649 m335%

Pm/c 1 ( not working )& EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR DEC- 02.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8882799808385687076.86204Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1991801911901720801529Dandy shower 4%

CP M/C III7676777599957219806079Dandy shower 1%

DP M/C IV5107153495495470680.03963Dandy shower 3%

EP M/C V4799672412785350880.03302Dandy shower 2%,starch prep.12%

TOTAL M/C284551781266742402321077

2PD PLANT26300263095249865.01710

3PULP MILL

ARDH12498012498851062355.56930

BFIBRE LINE664966490

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP47104710

BEVAPORATORS12922012922951227670.99158

CLFB 47444

ia) S/B186018600

iib) B/L HEATER180018000

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING2172170

DLFB 58040

ia) S/B200020000

iib) B/L HEATER180018000

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING6736730

TOTAL SRP

5CFB INTERNAL893308933958486958486

6TURBINE203220203221002032210020322

7CBD115001150558558

8STEAM BLOW2462460

GRAND TOTAL11613823627925118506464.1674519

Water used for Steam Generation =Steam Generated + CBD Losses

1161381149881150

Expected Return Condensate =85064 M3

Actual Return Condensate =74519 m364.16%

Actual DM Water Make up =41619 m335.84%

Targeted DM Water Make up =40649 m335%

Pm/c 1 ( not working )& EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR JAN- 03.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I9021812820985697880.06567Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II2281912190901971851862Dandy shower 4%

CP M/C III7639767563957185806050Dandy shower 1%

DP M/C IV4946148479895455882.03934Dandy shower 3%

EP M/C V4653558409585348185.03481Dandy shower 2%,starch prep.12%

TOTAL M/C285401685268552417321894

2PD PLANT20140201495191380.01611

3PULP MILL

ARDH12229012229851039558.77172

BFIBRE LINE678267820

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP48634863

BEVAPORATORS13181013181951252269.48684

CLFB 47622

ia) S/B201520150

iib) B/L HEATER182918290

iiic) DEAERATOR201502015951914951914

ivd) AIR HEATER155101551951473951473

ve) LINE FLUSHING2122120

DLFB 58027

ia) S/B182918290

iib) B/L HEATER201520150

iiic) DEAERATOR195301953951855951855

ivd) AIR HEATER201502015951914951914

ve) LINE FLUSHING2152150

TOTAL SRP

5CFB INTERNAL898608986958537958537

6TURBINE206290206291002062910020629

7CBD115301153558558

8STEAM BLOW3353350

GRAND TOTAL11650023671928298538365.0175741

Water used for Steam Generation =Steam Generated + CBD Losses

1165001153471153

Expected Return Condensate =85383 M3

Actual Return Condensate =75741 m365.01%

Actual DM Water Make up =40759 m334.99%

Targeted DM Water Make up =40775 m335%

Pm/c 1 ( not working )& EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen.Manager (PB)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR FEB- 03.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8100729737185626580.05897Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II2041821959901763851665Dandy shower 4%

CP M/C III6292636229958768804983Dandy shower 1%

DP M/C IV4308129417995397082.03427Dandy shower 3%

EP M/C V4195587360885306784.03031Dandy shower 2%,starch prep.12%

TOTAL M/C249361590233462383319003

2PD PLANT29200292095277485.02482

3PULP MILL

ARDH1083701083785921153.05742

BFIBRE LINE597559750

CCHLORINE GASSIFIER106910690

DClO2 PLANT822626196

P/MILL TOTAL

4S.R. PLANT

ACSP416941690

BEVAPORATORS11485011485951091175.08613

CLFB 46888

ia) S/B173617360

iib) B/L HEATER173217320

iiic) DEAERATOR148401484951410951410

ivd) AIR HEATER168001680951596951596

ve) LINE FLUSHING2562560

DLFB 57224

ia) S/B193619360

iib) B/L HEATER168016800

iiic) DEAERATOR168001680951596951596

ivd) AIR HEATER176401764951676951676

ve) LINE FLUSHING1641640

TOTAL SRP

5CFB INTERNAL804008040957638957638

6TURBINE194960194961001949610019496

7CBD104101041552552

8STEAM BLOW2702700

GRAND TOTAL10517221203839698019365.9069304

Water used for Steam Generation =Steam Generated + CBD Losses

1051721041311041

Expected Return Condensate =80193 M376.25%

Actual Return Condensate =69304 m365.90%

Actual DM Water Make up =35868 m334.10%

Targeted DM Water Make up =36810 m335%

Pm/c 1 ( not working )& EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen.Manager (PB)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR MARCH- 03.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8580.0Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II9085Dandy shower 4%

CP M/C III9580Dandy shower 1%

DP M/C IV9582.0Dandy shower 3%

EP M/C V8584.0Dandy shower 2%,starch prep.12%

TOTAL M/C

2PD PLANT9585.0

3PULP MILL

ARDH8553.0

BFIBRE LINE

CCHLORINE GASSIFIER

DClO2 PLANT

P/MILL TOTAL

4S.R. PLANT

ACSP

BEVAPORATORS9575.0

CLFB 4

ia) S/B

iib) B/L HEATER

iiic) DEAERATOR9595

ivd) AIR HEATER9595

ve) LINE FLUSHING

DLFB 5

ia) S/B

iib) B/L HEATER

iiic) DEAERATOR9595

ivd) AIR HEATER9595

ve) LINE FLUSHING

TOTAL SRP

5CFB INTERNAL9595

6TURBINE100100

7CBD55

8STEAM BLOW

GRAND TOTAL1051720065.90

Water used for Steam Generation =Steam Generated + CBD Losses

1051721041311041

Expected Return Condensate =80193 M376.25%

Actual Return Condensate =69304 m365.90%

Actual DM Water Make up =35868 m334.10%

Targeted DM Water Make up =36810 m335%

Pm/c 1 ( not working )& EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen.Manager (PB)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR OCT- 02.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I9536858867885737680.06942Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II2134852049901844801639Dandy shower 4%

CP M/C III7637767561957183806049Dandy shower 1%

DP M/C IV4835145469095445680.03752Dandy shower 3%

EP M/C V4798672412685350780.03301Dandy shower 2%,starch prep.12%

TOTAL M/C2894018362710421683

2PD PLANT35740357495339540.01430

3PULP MILL

ARDH12494012494851062036.74584

BFIBRE LINE575857580

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP48514851

BEVAPORATORS14173014173951346468.49701

CLFB 47669

ia) S/B186018600

iib) B/L HEATER170517050

iiic) DEAERATOR176701767951679951679

ivd) AIR HEATER180001800951710951710

ve) LINE FLUSHING5375370

DLFB 57872

ia) S/B200020000

iib) B/L HEATER180018000

iiic) DEAERATOR180001800951710951710

ivd) AIR HEATER176701767951679951679

ve) LINE FLUSHING5055050

TOTAL SRP

5CFB INTERNAL888708887958443958443

6TURBINE213780213781002137810021378

7CBD117901179559559

8STEAM BLOW1441440

GRAND TOTAL11905822887961718850362.2074056

Water used for Steam Generation =Steam Generated + CBD Losses

1178791179119058

Expected Return Condensate =88503 M383.73%

Actual Return Condensate =74056 m362.20%

Actual DM Water Make up =43427 m337.48%

Targeted DM Water Make up =41670 m335%

Pm/c 1 & EVP 3 (not working) are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR MARCH- 03.

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8491764772785656880.05254Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1744701674901507801206Dandy shower 4%

CP M/C III7537757462957089805671Dandy shower 1%

DP M/C IV4903147475695451880.03614Dandy shower 3%

EP M/C V4676655402185341880.02734Dandy shower 2%,starch prep.12%

TOTAL M/C273511711256402310018479

2PD PLANT28020280295266291.02423

3PULP MILL

ARDH12119012119851030180.09695

BFIBRE LINE597359730

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP377837780

BEVAPORATORS15516015516951474060.49373

CLFB 47662

ia) S/B201520150

iib) B/L HEATER182918290

iiic) DEAERATOR201502015951914951914

ivd) AIR HEATER155101551951473951473

ve) LINE FLUSHING2522520

DLFB 58069

ia) S/B182918290

iib) B/L HEATER201520150

iiic) DEAERATOR195301953951855951855

ivd) AIR HEATER201502015951914951914

ve) LINE FLUSHING2572570

TOTAL SRP

5CFB INTERNAL883008830958389958389

6TURBINE212710212711002127110021271

7CBD130901309565565

8STEAM BLOW4474470

GRAND TOTAL11726621997952698768465.5476851

Water used for Steam Generation =Steam Generated + CBD Losses

1159571309117266

Expected Return Condensate =87684 M374.77%

Actual Return Condensate =76851 m365.54%

Actual DM Water Make up =40415 m334.46%

Targeted DM Water Make up =41043 m335%

Pm/c 1 ( not working ) & EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR JUNE - 03

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8410757765385650570.05357Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1806721734901561801387Dandy shower 4%

CP M/C III7485757410957040805928Dandy shower 1%

DP M/C IV3643109353495335760.02120Dandy shower 3%

EP M/C V4491629386285328380.03090Dandy shower 2%,starch prep.12%

TOTAL M/C258351642241932174617882

2PD PLANT25910259195246130.0738

3PULP MILL

ARDH89250892585758639.63006

BFIBRE LINE664166410

CCHLORINE GASSIFIER117011700

DClO2 PLANT900660240

P/MILL TOTAL

4S.R. PLANT

ACSP367336730

BEVAPORATORS14525014525951379975.010352

CLFB 47402

ia) S/B201520150

iib) B/L HEATER192219220

iiic) DEAERATOR155101551951473951473

ivd) AIR HEATER170501705951620951620

ve) LINE FLUSHING2092090

DLFB 57835

ia) S/B192219220

iib) B/L HEATER198419840

iiic) DEAERATOR213902139952032952032

ivd) AIR HEATER155101551951473951473

ve) LINE FLUSHING2392390

TOTAL SRP

5CFB INTERNAL740807408957038957038

6TURBINE171220171221001712210017122

7CBD104601046552552

8STEAM BLOW6176170

GRAND TOTAL10569022694829967640259.4162788

Water used for Steam Generation =Steam Generated + CBD Losses

1046441046105690

Expected Return Condensate =76402 M372.28%

Actual Return Condensate =62788 m359.41%

Actual DM Water Make up =42902 m340.59%

Targeted DM Water Make up =36992 m335%

Pm/c 1 ( not working ) & EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR MAY-03

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I8631777785485667680.06283Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II1931771854901669801483Dandy shower 4%

CP M/C III5739575682955398804546Dandy shower 1%

DP M/C IV4811144466795443460.02800Dandy shower 3%

EP M/C V4727662406585345580.03252Dandy shower 2%,starch prep.12%

TOTAL M/C258391717241222163218364

2PD PLANT28980289895275330.0867

3PULP MILL

ARDH1108201108285942034.23795

BFIBRE LINE609160910

CCHLORINE GASSIFIER120912090

DClO2 PLANT930682248

P/MILL TOTAL

4S.R. PLANT

ACSP371037100

BEVAPORATORS13499013499951282470.19998

CLFB 47657

ia) S/B150015000

iib) B/L HEATER210021000

iiic) DEAERATOR207002070951967951967

ivd) AIR HEATER186001860951767951767

ve) LINE FLUSHING1271270

DLFB 56815

ia) S/B150015000

iib) B/L HEATER159015900

iiic) DEAERATOR177001770951682951682

ivd) AIR HEATER156001560951482951482

ve) LINE FLUSHING3933950

TOTAL SRP

5CFB INTERNAL950509505959030959030

6TURBINE233700233701002337010023370

7CBD21750217551095109

8STEAM BLOW107810780

GRAND TOTAL11585821699941598603662.5272431

Water used for Steam Generation =Steam Generated + CBD Losses

1136832175115858

Expected Return Condensate =86036 M374.25%

Actual Return Condensate =72431 m362.52%

Actual DM Water Make up =43427 m337.48%

Targeted DM Water Make up =40550 m335%

Pm/c 1 ( not working ) & EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR THE MONTH OF NOV-05

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I85Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II90Dandy shower 4%

CP M/C III95Dandy shower 1%

DP M/C IV95Dandy shower 3%

EP M/C V85Dandy shower 2%,starch prep.12%

TOTAL M/C

2PD PLANT95

3PULP MILL

ARDH85

BFIBRE LINE

CCHLORINE GASSIFIER

DClO2 PLANT

P/MILL TOTAL

4S.R. PLANT

ACSP

BEVAPORATORS95

CLFB 4

ia) S/B

iib) B/L HEATER

iiic) DEAERATOR95

ivd) AIR HEATER95

ve) LINE FLUSHING

DLFB 5

ia) S/B

iib) B/L HEATER

iiic) DEAERATOR95

ivd) AIR HEATER95

ve) LINE FLUSHING

TOTAL SRP

5CFB INTERNAL95

6TURBINE100

7CBD5

8STEAM BLOW

GRAND TOTAL

Water used for Steam Generation =Steam Generated + CBD Losses

Expected Return Condensate =

Actual Return Condensate =

Actual DM Water Make up =

Targeted DM Water Make up =

Pm/c 1 ( not working ) & EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

check list

Gen.Manager ( PB)

J.K.PAPER MILLS:JAYKAYPUR

POWER BLOCK

FRESH WATER WASTAGES,LOSSESS & LEAKAGES CHECK LIST

SL NOCHECKING POINTSOVER FLOWSDRAINAGELEAKAGESREMARKS

21" Pipe line

112 mw cooling tower

25.4 mw cooling tower

3Dm plant (old) degassor sump

4Dm plant (new) degassor sump

5Evaporator -3 cooling tower

6Pm/c no: 1 ADKA

7Pm/c no: 1 Hydropulper

8Pm/c no: 2 Hydropulper

9Singapur road railway station

10Mist chamber

18" pipe line

1Pm/c no:3 warm water tank

2Pm/c no:3 Hydropulper

3Pm/c no: 4 warm water tank

4Pm/c no: 4 Hydropulper

5Pm/c no: 5 warm water tank

6Pm/c no: 5 Hydropulper

7PD plant ( new) warm water tank

8PD plant vacuum pump

9Clo2 plant cooling tower : 1

10Clo2 plant cooling tower : 2

11Clo2 plant filters and storage tank

12Clo2 plant chilled tank

13Reclaimation plant old reservoir

14Reclaimation plant new reservoir

15Fiber line warm water tank

16Atlas capco compressor

17Admn building & Gardening

18techincal building

19Drinking water make up

20Bada chandili

Signature

Date :Time :

Blank

POWER BLOCK

9/11/00

ACTION PLAN FOR MONITORING THERMAL EFFICIENCY OF INDIVIDUAL BOILERS

DESCRIPTIONTARGET

1) INSTALLATION OF WEIGHTOMETERDEC.2000

ON CONVEYOR BELT BC -4A

2) INDIVIDUAL BOILER EFFICIENCYJan-01

CALCULATIONS

Gen.Manager (Power Block)

POWER BLOCK

9/12/00

ACTION PLAN FOR REDUCING BOILER HOUSE DISCHRGE WATER TEMP.

WE HAVE REDUCED THE BOILER BLODOWN WATER FROM 3% TO 1%

BY IMPROVING QUALITY OF D M WATER ,BY PROCESSING OLD DM PLANT

WATER THROW NEW DM PLANT MIXED BED FROM 17-07-2000.

HENCE THE TEMPERATURE OF THE WATER GOING OUT OF BOILER

HOUSE REDUCED TO 38 DEG.C FROM 40 DEG.C

Gen.Manager(Power Block)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR THE YEAR 2001 - 2002

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I12331711098112219859538668.076265Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II19881795190869017177499393Dandy shower 4%

CP M/C III909879109007795855734641495Dandy shower 1%

DP M/C IV50385151248873954642944.021509Dandy shower 3%

EP M/C V59437832151116854344951.026216Dandy shower 2%,starch prep.12%

TOTAL M/C34400722636321371288014174878

2PD PLANT36996036996953514641.515335

3PULP MILL

ARDH14090401409048511976831.043672

BFIBRE LINE77681776810

CCHLORINE GASSIFIER14066140660

DClO2 PLANT1078179202861

P/MILL TOTAL

4S.R. PLANT

ACSP6009360093

BEVAPORATORS15458501545859514685663.998781

CLFB 471162

ia) S/B16839168390

iib) B/L HEATER16755167550

iiic) DEAERATOR1590001590095151058513515

ivd) AIR HEATER1709801709895162438514533

ve) LINE FLUSHING457045700

DLFB 586446

ia) S/B17406174060

iib) B/L HEATER21664216640

iiic) DEAERATOR2119302119395201338518014

ivd) AIR HEATER2101002101095199598517858

ve) LINE FLUSHING517351730

TOTAL SRP

5CFB INTERNAL9914209914295941859594185

6TURBINE2581270258127100258127100258127

7CBD1390001390056955695

8STEAM BLOW638763870

GRAND TOTAL137427727119011030871014231749593

Water used for Steam Generation =Steam Generated + CBD Losses

1374277136037713900

Expected Return Condensate =1014231 M3

Actual Return Condensate =749593 m354.54%

Actual DM Water Make up =624684 m345.46%

Targeted DM Water Make up =618425 m345%

Pm/c 1 & EVP 3 (not working) are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

J.K.PAPER MILLS, JAYKAYPUR

POWER BLOCK

RETURN CONDENSATE BALANCE FOR

S.NO.PARTICULARSSTEAMCONDENSATEREMARKS

TOTALDIRECTINDIRECTEXPECTEDACTUAL

1PAPER MACHINES%m3%m3

AP M/C I85Dandy 1%,calender0.5%starch prep.7.5%

BP M/C II90Dandy shower 4%

CP M/C III95Dandy shower 1%

DP M/C IV95Dandy shower 3%

EP M/C V85Dandy shower 2%,starch prep.12%

TOTAL M/C

2PD PLANT95

3PULP MILL

ARDH85

BFIBRE LINE

CCHLORINE GASSIFIER

DClO2 PLANT

P/MILL TOTAL

4S.R. PLANT

ACSP

BEVAPORATORS95

CLFB 4

ia) S/B

iib) B/L HEATER

iiic) DEAERATOR95

ivd) AIR HEATER95

ve) LINE FLUSHING

DLFB 5

ia) S/B

iib) B/L HEATER

iiic) DEAERATOR95

ivd) AIR HEATER95

ve) LINE FLUSHING

TOTAL SRP

5CFB INTERNAL95

6TURBINE100

7CBD5

8STEAM BLOW

GRAND TOTAL

Water used for Steam Generation =Steam Generated + CBD Losses

1159571309117266

Expected Return Condensate =87684 M374.77%

Actual Return Condensate =76851 m365.54%

Actual DM Water Make up =40415 m334.46%

Targeted DM Water Make up =41043 m335%

Pm/c 1 ( not working ) & EVP 3 are having Flow Meters and rest on assumptions.

(Flash losses=10%,Trap losses=5% consedered)

Gen Manager (Power Block)

2,5 MWTG

J.K PAPER MILLS : JAYKAYPUR

POWER BLOCK

TURBINE EFFICIENCY FOR 2.5 MWTG FOR THE MONTH OFAPRIL 2001

TARGETEfficency: 46.5 + / - 1.5 %

Steam / KWh: 8.0 + / - 0.5 Kg / Kwh

INPUT DATA

STEAMPressureTemperatureEnthalpyQuantity

UNITKg / Cm2oCKCal / KgMT

H.P3540877413855

L.P3.219067711427

Condensate-0.850502428

Power Generated :1533000KWh

ENERGY INPUT

By L.P Extraction :(774-677)*11427*1000/860=1288859KWh

Equivalent H.P Steam :1288859*860 / 774*1000=1440Tons

By Condesate :(774-50)*2428*1000/860=2044037KWh

Total :=3332897KWh

EFFICIENCY

Efficiency =1533000=46.00%

3332897

STEAM / KWh

Steam / KWh =13855000=9.04Kg / KWH

1533000

5.4 MWTG

J.K PAPER MILLS : JAYKAYPUR

POWER BLOCK

TURBINE EFFICIENCY FOR 5.4 MWTG FOR THE MONTH OFAPRIL 2001

TARGETEfficency: 42.0 + / - 1.5 %

Steam / KWh: 9.4 + / - 0.5 Kg / Kwh

INPUT DATA

STEAMPressureTemperatureEnthalpyQuantity

UNITKg / Cm2oCKCal / KgMT

H.P3540077033112

M.P10.528071513061

L.P3.619067711034

Condensate-0.8250509017

Power Generated :3486290KWh

ENERGY INPUT

By M.P Extraction :(770-715)*13061*1000/860=835297KWh

Equivalent H.P Steam :835297*860 / 770*1000=933Tons

By L.P Extraction :(770-677)*11034*1000/860=1193212KWh

Equivalent H.P Steam :1193212*860 / 770*1000=1333Tons

By Condesate :(773-50)*9017*1000/860=7549116KWh

Total :=9577624KWh

EFFICIENCY

Efficiency =3486290=36.40%

9577624

STEAM / KWh

Steam / KWh =33112000=9.50Kg / KWH

3486290

12 MWTG

J.K PAPER MILLS : JAYKAYPUR

POWER BLOCK

TURBINE EFFICIENCY FOR 12 MWTG FOR THE MONTH OF APRIL 2001

TARGETEfficency: 42.0 + / - 1.5 %

Steam / KWh: 9.7 + / - 0.5 Kg / Kwh

INPUT DATA

STEAMPressureTemperatureEnthalpyQuantity

UNITKg / Cm2oCKCal / KgMT

H.P3440677371042

M.P1633874513639

L.P322569542538

Condensate-0.6757514865

Power Generated :7223800KWh

ENERGY INPUT

By M.P Extraction :(773-745)*13639*1000/860=444060KWh

Equivalent H.P Steam :444060*860 / 773*1000=494Tons

By L.P Extraction :(773-695)*42538*1000/860=3858098KWh

Equivalent H.P Steam :3858098*860 / 773*1000=4292Tons

By Condesate :(773-75)*14865*1000/860=12064849KWh

Total :=16367007KWh

EFFICIENCY

Efficiency =7223800=44.14%

16367007

STEAM / KWh

Steam / KWh =71042000=9.83Kg / KWH

7223800

Boiler Water Treatment Chemical (Conditioning Chemical) For Boiler water treatment the following Chemicals are used:1. Indion-5203( Filming Amine): used as 8 PPM on Make up Water.2. Indion-5164(pH Booster): used as a Contingency Chemical.Depending on the pH in Boiler water it is dosed as 1 to 2 PPM on Make up Water.3. Hydrazine Hydrate: used as Passivation When Boilers are in Ideal Conditions.

Cooling tower Treatment Chemical There are 3 Nos of Cooling towers:Three Cell Cooling towerFour Cell Cooling towerSingle Cell Cooling towerFollowing chemicals are used :Anti scaling & AnticorrosionBio despersentBiocidesSulphuric Acid

Cooling tower Water quality pH = 7.8 to 8.0 COC = 3 to 5

12MW COOLING TOWER FILL DEPOSIT CLEANING We are planning to remove the fill deposit with NALCO Chemicals :1. Nalco 73550 : This is a Biodetergent . It will remove the deposits through a combination of Chemical solubilization and Physical scrubbing .2. Nalco 90001 : Quaternary ammonium biocide.3. Sodium Hypochlorite : As per the system requirement.

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