washers rev11

8/8/2019 Washers Rev11

1/193

Washers

Section Knotters and Washers

V= Wash liquid of filtrate flow, t/t fiber

Washer CBF

V1 #NAME?y1 #NAME?Mass Flow #NAME? kg/sWater #NAME? kg/sFiber #NAME? kg/sConsistency #NAME? %

Temperature #NAME? C#NAME? Dissolved Substa #NAME?kg/s ###

DS% #NAME?

Lo #NAME?xo #NAME?Mass flow #NAME? kg/sConsistency #NAME? %Fiber #NAME? kg/sDissolved Substa #NAME?kg/s ###

Sf #NAME?DS % #NAME?

Temperature #NAME? Simulation Parameters

Filtrate concentration 0

Washed Pulp concentrate 18

Typical_Washed Concentration 18

Typical_Diln_Factor 2.3

Typical_Displacement_Ratio 0.7

Typical_Breakthrough_WR 0.3


2/193

Heat Loss 1

Ls - Ld DF #NAME? P Dilution Factor 7.18

(DF+Ld)/Ld Wash Ratio #NAME? P Wash_Ratio 2.58

DR [] #NAME? P Displacement_Ratio 0.81

#NAME? EquivalentDispRatio 0.86

Norden Number 2.14

Wash ratio

Weight ratio Calculated ParametersWash liquor ratio, R #NAME?

Dilution Factor Weight liquor ratio, W #NAME?

DF (V1-Lo) #NAME?

Displacement Ratio (V2-L1) #NAME?

DR

(xo-x1) #NAME?

(xo-y2) #NAME?DR #NAME?

(xo-x1) #NAME?

(xo-y2) #NAME?

DR #NAME?

Washing EfficiencyVerification of V2 and L1 #NAME?

Washing Efficiency `

Washing Yield

Y ( according mass balance) #NAME?E known 0.7

Y (R 1 W) #NAME?

Y (R=W=1) #NAME?

Y (Lo =Ln) #VALUE!

Washing efficiencyas defined as:

Washing yieldaccording to mass balance is the following:

The washing yieldof a washer with known E- value is as follows:


3/193

Fresh water #NAME?


4/193

V2 #NAME?y2 #NAME?Mass Flow #NAME? kg/sWater #NAME? kg/sFiber #NAME? kg/sConsistency #NAME? %

Temperature #NAME? CDissolved Substance #NAME?kg/sLs #NAME?

Ss #NAME?DS % #NAME?

L1 #NAME?x1 #NAME?Mass Flow #NAME? kg/sConsistency 18 %Fiber #NAME? kg/sDissolved Substance #NAME?kg/s

Ld 4.6Sd #NAME?DS % 12.47

Temperature #NAME?


5/193

P

v Filtrate liquor leaving per unit of liquor entering unwashed pulp.

P

P

P Fraction of dissolved solids removed

Difference of wash liquor entering minus liquor leaving withunwashed pulp divided by the amount of pulp washed.


6/193


7/193

Washers



Washer CBF

V1 28 t/t fibery1 135.4189 kg/tonMass Flow 167.9 kg/sWater 145.1593 kg/sFiber 0.0016 kg/sConsistency 0.0010 %

Temperature 99.92 CDissolved Substanc 22.74kg/sDS% 13.54

Total of liquor 167.8955

Lo 29.19 t/t fiberxo 131.1588 kg/tonMass flow 178.0 kg/sWater 148.8 kg/sConsistency 3.3 %Fiber 5.9 kg/s

Dissolved Substanc 23.3kg/sDS % 13.6 %

Temperature 101.8 C Simulation Param Total of liquor 172.1 kg/s

Filtrate concentration

Washed Pulp concentrate

Typical_Washed Concentration

Typical_Diln_Factor

Typical_Displacement_Ratio

Typical_Breakthrough_WR


8/193

Heat Loss

Dilution Factor

Wash_Ratio

Displacement_Ratio

EquivalentDispRatio

Norden Number

Calculated ParamWash liquor ratio, R

Weight liquor ratio, W

DF (V1-Lo)

(V2-L1)

DR

(xo-x1)

(xo-y2)DR

(xo-x1)

(xo-y2)

DR

Washing EfficieVerification of V2 and L1

Washing Efficiency

Washing Yield

Y ( according mass balance)E known

Y (R 1 W)

Y (R=W=1)

Y (Lo =Ln)

Dilution to blow tanks

Fiber 0

Temp 98.05

Flow 114.21


9/193

% Ds 13.41

To tank farm

% Dissolved solids 13.41

Mass flow 4.67

Temperature 98.05

Fresh water

Flow 28.21 kg/s

Temperature 94 C

Fresh water 80


10/193


11/193

V2 3.839 t/t fibery2 ###Mass Flow 22.63 kg/sWater 19.6704 kg/sConsistency 0.0050 %Fiber 0.0011 kg/sDissolved Substance 2.9614kg/sDS % 13.0852

Temperature 82.9 C

Total of liquor 22.63 kg/sLs 3.84

L1 4.56 t/t fiberx1 133.1 kg/tonMass Flow 32.8 kg/sWater 23.3 kg/sConsistency 18.0 %Fiber 5.9 kg/s

Dissolved Substance 3.574kg/sDS % 13.3

ters Temperature 91.6 Total of liquor 26.9 kg/s

#NAME?Ld 4.56#NAME?

#NAME?

#NAME?

#NAME?

#NAME?


12/193

0.35

1.08

0.61

0.74

2.26

eters0.8426 P

0.9754v Filtrate liquor leaving per unit of liquor entering unwashed pulp.

-0.7170P

-0.7170P

-1.905

0.307-0.015

0.259

10.264

0.54 P Fraction of dissolved solids removed

ncy-24.6380485

`

87.590.7

0.08

#VALUE!

#VALUE!

Pulp to Screens

Fiber 5.65

Temp 50.17

Flow 231.74

Difference of wash liquor entering minus liquor leaving withunwashed pulp divided by the amount of pulp washed.


13/193

Consistency 2.58

%DS 1.39


14/193


15/193

Washers



Washer 1A

V1 #NAME?y1 #NAME?Mass Flow #NAME? kg/s

Water #NAME? kg/s

Fiber #NAME? kg/s

Consistency #NAME? %

Temperature #NAME?C

Dissolved Substan #NAME?kg/s

DS % #NAME?

Lo #NAME?xo #NAME?Mass flow #NAME? kg/s


Fiber #NAME? kg/s


Sf #NAME?

DS % #NAME?

Temperature #NAME?C Simulation Parameters

Filtrate concentration #NAME?

Washed Pulp concentrate #NAME?

Typical_Washed Concentration #NAME?

Typical_Diln_Factor #NAME?

Typical_Displacement_Ratio #NAME?

Typical_Breakthrough_WR #NAME?


16/193

Heat Loss 0

Ls - Ld DF #NAME? P Dilution Factor #NAME?

(DF+Ld)/Ld Wash Ratio #NAME? P Wash_Ratio #NAME?

DR [] #NAME? P Displacement_Ratio #NAME?

EquivalentDispRatio #NAME?

Norden Number #NAME?

Wash ratio

Weight ratio Calculated ParametersWash ratio, W #NAME?

Dilution Factor Weight ratio, R #NAME?

DF (V1-Lo) #NAME?


DR

(xo-x1) #NAME?


(xo-x1) #NAME?

(xo-y2) #NAME?

DR #NAME?


Washing Efficiency #NAME?

Washing Yield


Y (R 1 W) #NAME?

Y (R=W=1) #NAME?

Y (Lo =Ln) #NAME?


Fiber #NAME?

Temp #NAME?

Flow #NAME?





17/193

% Ds #NAME?

To tank farm

% Dissolved solids #NAME?

Mass flow #NAME?

Temperature #NAME?

Fresh water #NAME?


18/193


Water #NAME? kg/s

Fiber #NAME? kg/s


Temperature #NAME? C

Dissolved Substance #NAME? kg/s

Ls #NAME?

Ss #NAME?DS % #NAME?

L1 #NAME?x1 #NAME?Mass Flow #NAME? kg/s


Fiber #NAME? kg/s

Dissolved Substance #NAME? kg/s

Ld #NAME?

Sd #NAME?

DS % #NAME?



19/193

P

v

P

P

P

Pulp to Screens

Fiber #NAME?

Temp #NAME?

Flow #NAME?


20/193

Consistency #NAME?


21/193

Washers



Washer 1A

V1 30.4 kg/tony1 130.8 kg/tonMass Flow 179.49 kg/s

Water 155.9966 kg/s

Consistency 0.0050 %

Fiber 0.0015 kg/s

Dissolved Substance 23.49kg/s

DS % 13.09

Temperature 70.5262 C

Total of liquor 179.4821kg/s

Lo 28.1 kg/tonxo 79.2 kg/tonMass flow 196.8kg/sWater 165.8kg/sConsistency 3.0%Fiber 5.9kg/sDissolved Substance 25.1kg/s

DS % 13.1%

Temperature 84.3C Simulation Parameters Total of liquor 190.9 kg/s

Filtrate concentration 0.01

Washed Pulp concentrate 12

Typical_Washed Concentration 12

Typical_Diln_Factor 2.3

Typical_Displacement_Ratio 0.72

Typical_Breakthrough_WR 0.3


22/193

Heat Loss 0

Dilution Factor -1.93

Wash_Ratio 0.74

Displacement_Ratio 0.53

EquivalentDispRatio 0.52

Norden Number 2.52

Calculated ParametersWash ratio, W 0.7362

Weight ratio, R 1.0824

DF (V1-Lo) 2.3186

(V2-L1) -1.9347

DR

(xo-x1) -31.738

(xo-y2) -42.248DR 0.751

(xo-x1) -12.607

(xo-y2) 0.988

DR 1.038

Washing EfficiencyVerification of V2 and L1 -25.0419872

Washing Efficiency -3.45

Washing Yield

Y ( according mass balance) 149.38E known 0.7

Y (R 1 W) -0.19

Y (R=W=1) 1.08

Y (Lo =Ln) 1.41


Fiber 0

Temp 98.05

Flow 114.21


23/193

% Ds 13.41

To tank farm

% Dissolved solids 13.41

Mass flow 4.67

Temperature 98.05

Fresh water

Flow 28.21 kg/s

Temperature 94 C


24/193

V2 5.4 kg/tony2 121.5 kg/tonMass Flow 31.83 kg/s

Water 27.9663 kg/s


Fiber 0.0015 kg/s


DS % 12.146

Temperature 70.53 C

Total of liquor 31.8326 kg/sLs 5.4

L1 7.33 t/t fiberx1 110.9 kg/tonMass Flow 49.14 kg/s

Water 37.79Consistency 12 %

Fiber 5.8964 kg/s


DS % 12.61

Temperature 76.98 C

Total of liquor 43.2405 kg/sLd 7.33


25/193

P

v

P

P

P

Pulp to Screens

Fiber 5.65

Temp 50.17

Flow 231.74


26/193

Consistency 2.58

%DS 1.39


27/193

Washers



Washer 2A


Water #NAME? kg/s

Fiber #NAME? kg/s




DS % #NAME?

Lo #NAME?

xo #NAME?

Mass flow #NAME? kg/s


Fiber #NAME? kg/s


Sf #NAME?

DS % #NAME?

Simulation Parameters








28/193

Heat Loss #NAME?






Wash ratio

Weight ratio Calculated ParametersWash ratio, W #NAME?

Dilution Factor Weight ratio, R #NAME?

DF (V1-Lo) #NAME?


DR

(xo-x1) #NAME?


(xo-x1) #NAME?

(xo-y2) #NAME?

DR #NAME?



Washing Yield


Y (R 1 W) #NAME?

Y (R=W=1) #NAME?

Y (Lo =Ln) #NAME?


Fiber #NAME?

Temp #NAME?

Flow #NAME?





29/193

% Ds #NAME?

To tank farm


Mass flow #NAME?

Temperature #NAME?

Fresh water #NAME? kg/s


30/193


Water #NAME? kg/s

Fiber #NAME? kg/s



Dissolved Substance #NAME?kg/s

Ls

Ss

DS % #NAME?

L1 #NAME?

x1 #NAME?

Mass Flow #NAME? kg/s


Fiber #NAME? kg/s

Dissolved Substance #NAME?kg/s

Ld #NAME?

Sd #NAME?

DS % #NAME?

Temperature #NAME?


31/193

P

v

P

P

P

Pulp to Screens

Fiber #NAME?

Temp #NAME?

Flow #NAME?


32/193

Consistency #NAME?


33/193

Washers



Washer 2A

V1 24 t/t fibery1 121.4509 kg/tonMass Flow 293.78 kg/s

Water 258.08 kg/s

Consistency 0.005 %

Fiber 0.01 kg/s

Dissolved Substanc 35.68kg/s

DS % 12.15

Temperature 71.22 C


Lo 25.92 t/t fiber

xo ###

Mass flow 311.1kg/sWater 267.9kg/sConsistency 1.9%Fiber 5.9kg/sDissolved Substa 37.3kg/s

DS % 12.2%

Temperature 71.5C Simulation Parameters Total of liquor 305.2kg/s

Filtrate concentration 0







34/193

Heat Loss #NAME?

Ls - Ld Dilution Factor #NAME?

(DF+Ld)/Ld Wash_Ratio #NAME?

Displacement_Ratio #NAME?



Wash ratio

Weight ratio Calculated ParametersWash ratio, W 0.1084

Dilution Factor Weight ratio, R 0.9444

DF (V1-Lo) -1.4418

Displacement Ratio (V2-L1) -21.8286

DR

(xo-x1) 960.932

(xo-y2) 884.303DR 1.087

(xo-x1) -52.751

(xo-y2) -3.761

DR -20.763


Washing Efficiency -0.06

Washing Yield

Y ( according mass balance) 10.68E known 0.7

Y (R 1 W) 0

Y (R=W=1) -0.07

Y (Lo =Ln) -0.07


Fiber #NAME?

Temp #NAME?

Flow #NAME?





35/193

% Ds #NAME?

To tank farm


Mass flow #NAME?

Temperature #NAME?



36/193

V2 2.653 t/t fibery2 96.7000 kg/tonMass Flow 31.83 kg/s

Water 28.7547 kg/s


Fiber 0.0015 kg/s

Dissolved Substance 3.0784 kg/s

DS % 9.670

Temperature 59.9 C


L1 ###

x1 20.1 kg/ton

Mass Flow 49.14 kg/s

Water 38.58Consistency 12 %

Fiber 5.8964 kg/s


DS % 10.78

Temperature 64.96 C

Total of liquor 44.4735 kg/s


37/193

P

v

P

P

P

Pulp to Screens

Fiber #NAME?

Temp #NAME?

Flow #NAME?


38/193

Consistency #NAME?


39/193

Washers



Washer 3A

V1 #NAME? V2y1 #NAME? y2

Mass Flow #NAME? kg/s Mass Flow

Water #NAME? kg/s Water

Fiber #NAME? kg/s Fiber

Consistency #NAME? % Consistency

Temperature #NAME? C Temperature

Dissolved Substan #NAME? kg/s Dissolved Substa

% DS #NAME? Ls

Ss

DS %

Lo #NAME? L1

xo #NAME? x1

Mass flow #NAME? kg/s Mass Flow

Consistency #NAME? % Consistency

Fiber #NAME? kg/s Fiber

Dissolved Substan #NAME? kg/s Dissolved Substa

Sf #NAME? Ld

DS % #NAME? Sd Temperature #NAME? C Simulation Parameters DS %








40/193

Heat Loss #NAME?






Wash ratio

Weight ratio Calculated ParametersWash ratio, W #NAME?P

Dilution Factor Weight ratio, R #NAME?v

DF (V1-Lo) #NAME? P

Displacement Ratio (V2-L1) #NAME? P

DR

(xo-x1) #NAME?

(xo-y2) #NAME?

DR #NAME?

(xo-x1) #NAME?

(xo-y2) #NAME?

DR #NAME?P



Washing Yield

Y ( according mass balance) #NAME?

E known 0.7

Y (R 1 W) #NAME?

Y (R=W=1) #NAME?

Y (Lo =Ln) #NAME?


Fiber #NAME?

Temp #NAME?

Flow #NAME?





41/193

% Ds #NAME?

To tank farm


Mass flow #NAME?

Temperature #NAME?

Fresh Water #NAME? kg/s


42/193

#NAME?#NAME?

#NAME? kg/s

#NAME? kg/s

#NAME? kg/s

#NAME?%

#NAME?C

ce #NAME? kg/s

#NAME?

#NAME?

#NAME?

#NAME?

#NAME?

#NAME? kg/s

#NAME?%

#NAME? kg/s

ce #NAME? kg/s

#NAME?

#NAME?#NAME?


43/193

Pulp to Screens

Fiber #NAME?

Temp #NAME?

Flow #NAME?


44/193

Consistency #NAME?


45/193

Washers



Washer 3A

V1 37.15 V2y1 0.1 y2Mass Flow 219 kg/s Mass FlowWater 197.81 kg/s WaterConsistency 0% ConsistencyFiber 0.01 kg/s FiberDissolved Substan 21.18 kg/s Dissolved Subst% DS 9.67 % DS %

Temperature 60.43 C Temperatur Total of liquor 218.99 kg/s Total of liquor

Lo 36.2 L1xo 41.8 x1Mass flow 236.3 kg/s Mass FlowWater 207.6 kg/s WaterConsistency 2.5 % ConsistencyFiber 5.9 kg/s FiberDissolved Substan 22.8 kg/s Dissolved Subst

DS % 9.9 % DS %

Temperature 60.9 C Simulation Parameters Temperature Total of liquor 230.4 kg/s Total of liquor








46/193

Heat Loss #NAME?

Dilution Factor #NAME?

Wash_Ratio #NAME?

Displacement_Ratio #NAME?



Calculated ParametersWash ratio, W 0.6586P

Weight ratio, R 1.0255v

DF (V1-Lo) 0.9250 P

(V2-L1) -1.9346 P

DR

(xo-x1) 1.484

(xo-y2) 41.811

DR 0.035

(xo-x1) 56.112

(xo-y2) #NAME?

DR #NAME?P



Washing Yield

Y ( according mass balance) 0.24

E known 0.7

Y (R 1 W) -0.04

Y (R=W=1) #NAME?

Y (Lo =Ln) #NAME?


Fiber #NAME?

Temp #NAME?

Flow #NAME?


47/193

% Ds #NAME?

To tank farm


Mass flow #NAME?

Temperature #NAME?



48/193

3.730

22kg/s22kg/s

%kg/s

nce kg/s#NAME?

40C22

5.6740.3339.30 kg/s31.82 kg/s15.00%

5.89kg/snce 1.58 kg/s

4.74

50.02C33.40 kg/s


49/193

Pulp to Screens

Fiber #NAME?

Temp #NAME?

Flow #NAME?


50/193

Consistency #NAME?


51/193

ID Typical parameters

Type of washer Vendor

DF DR

Washer

46-5166 CBF Washer Vaccum Drum Filter 2.3000 0.7200 0.0300

Washer

46-5101 Washer 1A Vaccum Drum Filter 2.3000 0.7200 0.0300

Washer

46-5101 Washer 1A Vaccum Drum Filter 2.3000 0.7200 0.0300

Washer 46-5101 Washer 1A Vaccum Drum Filter 2.3000 0.7200 0.0300

Knotters &

Washratio, W

Weightratio, R

Breakthrough,WR

Modifie

Efficien

Increase FW-94-80

Capacity and efficiency of the wash press depend on the following parameters:-Consistency of inlet pulp-Vat pressure-Drum speed

-Drum torque-Flow of wash liquor-Drainage properties of the pulp.


52/193


53/193

positivo

Inlet

Water V2 Y2 Pulp stream, % DS Wa

0.58-0.77 13.0852 2.9614 19.6704 22.6330 3.8388 130.8518 13.5652 23.3488 148.7

0.58-0.77 4.0 -6.0 12.1457 3.8663 27.9663 31.8342 5.3986 121.4572 13.1335 25.0705 165.8

0.58-0.77 4.0 -6.0 9.6705 3.0784 28.7547 31.8348 5.3987 96.7048 12.2111 37.2646 267.9

0.58-0.77 4.0 -6.0 #NAME? 0.0000 22.0000 22.0000 3.7321 0.0000 9.8796 22.7617 207.6

Bleaching Do + Eop

-4.2273

-0.72

Equivalent Displacementratio, EDR

Norden efficiencyratio, E

Shower,% DS

Dissolvedsolids kg/s

Shower,Flow

DissolvedSubstance

Pulp stream,k /s


54/193


55/193

Outlet

Lo Xo Water V1 Y1 Water Pulp fiber

3.3123 29.1936 135.6519 13.54 22.74 145.16 167.90 28.48 135.42 13.3064 3.5740 23.2852 5.8959 32.7550

3.0000 32.3738 131.3350 13.09 23.49 156.00 179.49 30.44 130.85 12.6070 5.4513 37.7892 5.8964 49.1370

1.8997 51.7550 122.1108 12.15 35.68 258.08 293.78 49.82 121.46 10.7849 4.6635 38.5771 5.8964 49.1370

2.4993 39.0833 98.7965 9.67 21.18 197.81 219.00 37.15 96.70 4.7443 1.5848 31.8193 5.8948 39.2990

positiv

Pulp stream%Cs

Shower,% DS

Dissolvedsolids, kg/s

Shower,Flow

Pulpstream, %DS

Dissolvedsolids,kg/s

Pulpstream,flow

Ps%


56/193


57/193

Calculated parameters

X1

133.0637 0.8427 0.9754 -0.7168 0.5392 #NAME? #NAME? #NAME? 0.7243

126.0698 0.7362 0.9402 -1.9347 0.5330 #NAME? #NAME? #NAME? 0.5710

107.8494 0.7362 0.9626 -1.9346 0.5613 #NAME? #NAME? #NAME? 0.5838

47.4430 0.6586 0.9505 -1.9346 #NAME? #NAME? #NAME? #NAME? #NAME?

Wash liquor

ratio, R

Weight liquor

ratio, W

Dilution

Factor, F

DR assuming %

(Cadsim)

Washing

efficiency as thearticle

Washing

efficiency asCadsim

Modified

efficiency factor,Est

Equivalent

DisplacemenRatio, EDR


58/193


59/193

ns Dilution to blowtanks To tank farm Above the typical valueCs% Flow Temp Ds % T

DF DR WR EDR

#####################

0.0000 0.0000 Good WR Good EDR

#####################

0.0000 0.0000 Good WR 0.0000

#####################

0.0000 0.0000 Good WR 0.0000

##################### 0.0000 #NAME? Good WR #NAME?

Flow

%DS


60/193


61/193

WashersType of washer Vendor

DF DR

Vaccum Drum Filter 0 0.72 0.03 2.5-4.0 0.58-0.77

Pressure Washer 0 0.72 0.03 0.08 - 0.85

Wash Press 0 0.72 0.03 0.83 -0.86Atmospheric Pressure - 1 Stage 0 0.72 0.03 3 - 5 .76 - 0.90

Atmospheric Pressure - 2 Stage 18 0.72 0.03 0.92 - 0.96

Pressure Diffuser 18 0.72 0.03 4.5 6.5 .87 - 0.92

References

1 Smook pag 105

2 Water reduction book

3

45

Wash ratio,W

Weightratio, R

Breakthrough, WR

ModifiedNordenEfficiency

ratio Est 1

EquivalentDisplacement ratio, EDR2


62/193


63/193

Washers

Data obtained every 30,000 seconds

Fresh Water CBF

Flow (m3/s) Temp. C % DS Filtra Yield % DS

13.54 0.84 -0.72 0.54 ### 0.84 #NAME? 0.72

22

40.00 13.54 0.84 -0.72 0.54 2.30 0.844 2.296 0.72

60.00 13.54 0.84 -0.72 0.54 2.30 0.844 2.296 0.72

70.00 13.54 0.84 -0.72 0.54 2.30 0.844 2.296 0.72

80.00 13.54 0.84 -0.71 0.54 2.30 0.84 2.30 0.72 4.11 -- 4 94.00 13.47 1.00 0.00 0.59 2.88 0.844 2.883 0.75

25 40.00 13.50 0.96 -0.19 0.58 2.28 0.844 2.277 0.75

60.00 13.50 0.96 -0.19 0.58 2.28 0.844 2.277 0.75

70.00 13.50 0.96 -0.19 0.58 2.28 0.844 2.277 0.75

80.00 13.50 0.96 -0.18 0.58 2.28 0.844 2.277 0.75

4.67 -- 4c 94.00 13.36 1.14 0.62 0.62 2.25 0.844 2.253 0.78

28 40.0 13.411 1.082 0.374 0.610 2.258 0.844 2.258 0.769 60.0 13.411 1.082 0.373 0.610 2.258 0.844 2.258 0.769 1

70.0 13.411 1.082 0.374 0.610 2.258 0.844 2.258 0.769 1

80.0 13.392 1.082 0.373 0.610 2.260 0.844 2.260 0.769 1

5.28 -- 4 94.0 13.172 1.284 1.293 0.658 2.243 0.844 2.243 0.799 1

32 40.000 13.250 1.228 1.038 0.645 2.247 0.844 2.247 0.791

60.000 13.250 1.228 1.038 0.645 2.247 0.844 2.247 0.791 70.000 13.250 1.228 1.038 0.645 2.247 0.844 2.247 0.791

80 000 13 21 1 226 1 03 0 64 2 25 0 84 2 25 0 79

Wash ratio,R

DilutionFactor, Df

DisplacementRatio,DR

ModifiedNordenEfficiency Factor,

Est

NordenEfficiency, E

EquivalentDisplacementRatio, EDR


64/193

12.15 0.74 -1.93 0.56 ### 0.86 #NAME? 0.58

7.71E-04 98.93 77.13 13.54 12.15 0.74 -1.93 0.56 2.88 0.86 2.88 0.58

7.71E-04 98.94 77.14 13.54 12.14 0.74 -1.93 0.56 2.88 0.86 2.88 0.58

7.71E-04 98.95 77.14 13.54 12.14 0.74 -1.93 0.56 2.88 0.86 2.88 0.58 7.70E-04 98.95 77.10 13.54 12.14 0.74 -1.93 0.56 2.88 0.86 2.88 0.58

8.10E-04 98.36 81.05 13.47 10.79 0.83 -1.24 0.60 2.88 0.86 2.88 0.63

8.00E-04 98.44 80.02 13.50 11.18 0.81 -1.43 0.59 2.88 0.86 2.88 0.62

8.00E-04 98.49 80.02 13.50 11.18 0.81 -1.43 0.59 2.88 0.86 2.88 0.62

8.00E-04 98.51 80.02 13.50 11.18 0.81 -1.43 0.59 2.88 0.86 2.88 0.62

8.00E-04 98.53 80.05 13.496 11.170 0.81 -1.42 0.59 2.88 0.86 2.88 0.62

8.44E-04 97.73 84.48 13.359 9.275 0.91 -0.64 0.64 2.89 0.86 2.89 0.66 8.31E-04 97.788 83.106 13.411 9.895 0.880 -0.881 0.625 2.886 0.858 2.886 0.648

8.30E-04 97.918 83.100 13.411 9.897 0.880 -0.881 0.625 2.886 0.858 2.886 0.648

8.31E-04 97.944 83.106 13.411 9.894 0.880 -0.881 0.625 2.886 0.858 2.886 0.648

8.31E-04 97.978 83.102 13.392 9.615 0.880 -0.878 0.626 2.876 0.858 2.876 0.648

8.81E-04 96.947 88.168 13.172 7.530 1.00 0.01 0.67 2.88 0.86 2.88 0.70

8.67E-04 96.802 86.7615 13.250 8.185 0.968 -0.238 0.660 2.902 0.858 2.902 0.683

8.67E-04 97.029 86.7616 13.250 8.185 0.968 -0.238 0.660 2.902 0.858 2.902 0.683 8.67E-04 97.142 86.7616 13.250 8.185 0.968 -0.238 0.660 2.902 0.858 2.902 0.683

8.67E-04 97.224 86.7131 13.208 7.710 0.967 -0.239 0.660 2.839 0.858 2.839 0.683

9.25E-04 95.982 92.5430 12.894 5.638 1.105 0.771 0.709 2.935 0.858 2.935 0.731

To tank farm Pulp to screensFiber Temp Flow % Ds Fiber Temp Flow % Ds Cs%


65/193

1.71E-05 131.88 36.09 12.75 5.99 48.04 231.74 1.54 2.58

1.71E-05 131.90 36.09 12.75 5.99 49.08 231.74 1.54 2.58

0.00 98.53 34.09 13.50 5.99 50.11 231.74 1.54 2.58

8.44E-04 97.73 84.48 13.36 5.99 50.20 231.74 1.34 2.58

1.71E-05 97.788 34.211 13.411 5.990 45.599 231.739 1.401 2.585

1.71E-05 131.223 36.210 12.683 5.990 47.915 231.741 1.401 2.585

1.71E-05 97.944 34.211 13.411 5.990 49.016 231.739 1.401 2.585

1.71E-05 97.979 34.210 13.393 5.986 50.137 231.714 1.401 2.584

### 96.947 34.396 13.172 5.990 50.300 231.739 1.221 2.585

1.72E-05 96.8 34.35 13.25 5.99 45.28 231.74 1.25 2.58

1.72E-05 97.03 34.35 13.25 5.99 47.76 231.74 1.25 2.58

1.72E-05 97.14 34.35 13.250 5.990 49.004 231.739 1.254 2.585

1.72E-05 97.22 34.34 13.208 5.989 50.233 231.731 1.229 2.584

1.73E-05 95.98 34.54 12.89 5.99 50.45 231.74 1.120 2.585


66/193


67/193


68/193


69/193


70/193


71/193

Washer 1A

Yield

0.53 #NAME? 0.77 #NAME? 0.57

0.53 2.52 0.77 2.52 0.57

0.53 2.52 0.77 2.52 0.57

0.53 2.52 0.77 2.52 0.57

0.53 2.52 0.77 2.52 0.57

0.57 2.50 0.77 2.50 0.61

0.56 2.50 0.77 2.50 0.60

0.56 2.50 0.77 2.50 0.60

0.56 2.50 0.77 2.50 0.60

0.56 2.50 0.77 2.50 0.60

0.60 2.49 0.77 2.49 0.63

0.590 2.494 0.773 2.494 0.623

0.590 2.494 0.773 2.494 0.623

0.590 2.494 0.773 2.494 0.623

0.590 2.494 0.773 2.494 0.623

0.632 2.490 0.773 2.490 0.662

0.621 2.490 0.773 2.490 0.652

0.621 2.490 0.773 2.490 0.652

0.621 2.490 0.773 2.490 0.652

Displa.Ratio,DR

ModifiedNorden

EfficiencyFactor, E

st

NordenEfficiency, E

EquivalentDisplacementRatio, EDR


72/193

#NAME? #NAME? 0.85 #NAME? #NAME?

0.52 2.85 0.85 2.85 0.64

0.52 2.85 0.85 2.85 0.64

0.52 2.85 0.85 2.85 0.640.52 2.86 0.85 2.86 0.64

0.58 2.85 0.85 2.85 0.69

0.56 2.84 0.85 2.84 0.68

0.56 2.84 0.85 2.84 0.68

0.56 2.84 0.85 2.84 0.68

0.56 2.83 0.85 2.83 0.68

0.62 2.86 0.85 2.86 0.720.6062 2.837 0.855 2.837 0.710

0.6062 2.837 0.855 2.837 0.710

0.6062 2.837 0.855 2.837 0.710

0.6068 2.817 0.855 2.817 0.710

0.6676 1.64 0.85 1.64 0.76

0.6516 2.852 0.855 2.852 0.745

0.6516 2.852 0.855 2.852 0.745

0.6516 2.852 0.855 2.852 0.745

0.6520 2.767 0.855 2.767 0.745

0.7131 2.874 0.855 2.874 0.792


73/193

60 C and 32


74/193


75/193

32 and 80


76/193

32 m3/s and 94 C


77/193


78/193


79/193


80/193


81/193


82/193


83/193


84/193


85/193


86/193


87/193


88/193


89/193


90/193


91/193


92/193


93/193


94/193

31 kg/s and 80


95/193


96/193


97/193


98/193


99/193


100/193

31 m3/s and 70


101/193


102/193


103/193


104/193


105/193


106/193

31 m3/s and 60


107/193


108/193


109/193


110/193


111/193


112/193


113/193


114/193


115/193

31 m3/s and 40


116/193


117/193


118/193

28.21 m3/h and 94


119/193


120/193


121/193


122/193


123/193


124/193

28.21 m3/h and 70


125/193


126/193


127/193

28.21 m3


128/193


129/193


130/193

/h and 60


131/193


132/193


133/193


134/193


135/193


136/193

28.21 m3/h and 40


137/193


138/193


139/193


140/193


141/193


142/193

28.21 m3/h and 80


143/193


144/193


145/193


146/193


147/193


148/193

28.21 m3/h and 70


149/193


150/193


151/193


152/193


153/193


154/193

28.21 m3/h and 60


155/193


156/193


157/193


158/193


159/193


160/193

28.21 m3/h and 40


161/193


162/193


163/193


164/193


165/193


166/193

22 kg/s and 80


167/193


168/193


169/193


170/193


171/193


172/193

22 m3/s and 70


173/193


174/193


175/193


176/193


177/193


178/193

22 m3/s and 60


179/193


180/193


181/193


182/193


183/193


184/193


185/193


186/193


187/193

22 m3/s and 40


188/193


189/193


190/193


191/193


192/193


193/193

washers rev11

Documents