- •Recovered Paper and Recycled Fibers
- •Isbn: 3-527-30999-3
- •Introduction
- •Isbn: 3-527-30999-3
- •Isbn: 3-527-30999-3
- •2006, Isbn 3-527-30997-7
- •Volume 1
- •Isbn: 3-527-30999-3
- •4.1 Introduction 109
- •4.2.5.1 Introduction 185
- •4.3.1 Introduction 392
- •5.1 Introduction 511
- •6.1 Introduction 561
- •6.2.1 Introduction 563
- •6.4.1 Introduction 579
- •Volume 2
- •7.3.1 Introduction 628
- •7.4.1 Introduction 734
- •7.5.1 Introduction 777
- •7.6.1 Introduction 849
- •7.10.1 Introduction 887
- •8.1 Introduction 933
- •1 Introduction 1071
- •5 Processing of Mechanical Pulp and Reject Handling: Screening and
- •1 Introduction 1149
- •Isbn: 3-527-30999-3
- •Isbn: 3-527-30999-3
- •Isbn: 3-527-30999-3
- •Isbn: 3-527-30999-3
- •Introduction
- •Introduction
- •Isbn: 3-527-30999-3
- •1 Introduction
- •1 Introduction
- •1 Introduction
- •1 Introduction
- •1 Introduction
- •1 Introduction
- •150.000 Annual Fiber Flow[kt]
- •1 Introduction
- •1 Introduction
- •Introduction
- •Isbn: 3-527-30999-3
- •Void volume
- •Void volume fraction
- •Xylan and Fiber Morphology
- •Initial bulk residual
- •4.2.5.1 Introduction
- •In (Ai) Model concept Reference
- •Initial value
- •Validation and Application of the Kinetic Model
- •Inititial
- •Viscosity
- •Influence on Bleachability
- •Impregnation
- •Impregnation
- •Impregnation
- •Impregnation
- •Impregnation
- •Impregnation
- •Impregnation
- •Impregnation
- •Impregnation
- •Impregnation
- •Introduction
- •International
- •Impregnation
- •Influence of Substituents on the Rate of Hydrolysis
- •140 116 Total so2
- •Xylonic
- •Viscosity Brightness
- •Xyl Man Glu Ara Furf hoAc XyLa
- •Initial NaOh charge [% of total charge]:
- •Introduction
- •Isbn: 3-527-30999-3
- •Introduction
- •Isbn: 3-527-30999-3
- •Introduction
- •Introduction
- •Isbn: 3-527-30999-3
- •In 1950, about 50% of the global paper production was produced. This proportion
- •4.0% Worldwide; 4.2% for the cepi countries; and 4.8% for Germany.
- •1150 1 Introduction
- •1 Introduction
- •1 Introduction
- •Virgin fibers
- •74.4 % Mixed grades
- •Indonesia
- •Virgin fibers
- •Inhomogeneous sample Homogeneous sample
- •Variance of sampling Variance of measurement
- •1.Quartile
- •3.Quartile
- •Insoluble
- •Insoluble
- •Insoluble
- •Integral
- •In Newtonion liquid
- •Velocity
- •Increasing dp
- •2Α filter
- •0 Reaction time
- •Increasing interaction of probe and cellulose
- •Increasing hydrodynamic size
- •Vessel cell of beech
- •Initial elastic range
- •Internal flow
- •Intact structure
- •Viscosity 457
- •Isbn: 3-527-30999-3
- •1292 Index
- •Visbatch® pulp 354
- •Index 1293
- •1294 Index
- •Impregnation 153
- •Viscosity–extinction 433
- •Index 1295
- •1296 Index
- •Index 1297
- •Inhibitor 789
- •1298 Index
- •Index 1299
- •Impregnation liquor 290–293
- •1300 Index
- •Industries
- •Index 1301
- •1302 Index
- •Index 1303
- •Xylose 463
- •1304 Index
- •Index 1305
- •1306 Index
- •Index 1307
- •1308 Index
- •In conventional kraft cooking 232
- •Visbatch® pulp 358
- •Index 1309
- •In prehydrolysis-kraft process 351
- •Visbatch® cook 349–350
- •1310 Index
- •Index 1311
- •1312 Index
- •Viscosity 456
- •Index 1313
- •Viscosity 459
- •Interactions 327
- •1314 Index
- •Index 1315
- •Viscosity 459
- •1316 Index
- •Index 1317
- •Xylose 461
- •Index 1319
- •Visbatch® pulp 355
- •Impregnation 151–158
- •1320 Index
- •Index 1321
- •1322 Index
- •Xylan water prehydrolysis 333
- •Index 1323
- •1324 Index
- •Viscosity 459
- •Index 1325
- •Xylose 940
- •1326 Index
- •Index 1327
- •In selected kinetics model 228–229
- •4OMeGlcA 940
- •1328 Index
- •Index 1329
- •Intermediate molecule 164–165
- •1330 Index
- •Viscosity 456
- •Index 1331
- •1332 Index
- •Impregnation liquor 290–293
- •Index 1333
- •1334 Index
- •Index 1335
- •1336 Index
- •Impregnation 153
- •Index 1337
- •1338 Index
- •Viscose process 7
- •Index 1339
- •Volumetric reject ratio 590
- •1340 Index
- •Index 1341
- •1342 Index
- •Index 1343
- •1344 Index
- •Index 1345
- •Initiator 788
- •Xylose 463
- •1346 Index
- •Index 1347
- •Vessel 385
- •Index 1349
- •1350 Index
- •Xylan 834
- •1352 Index
1302 Index
– theory 579–586
cleavage, polysaccharide chain 662–666
CLF see continuous liquor flow
ClO2 see chlorine dioxide
closed rotor 564
closure, degree of 893
CMP see chemimechanical pulp
CO3
2– see carbonate ion
coarse material, refiner process 1115
coarseness 1275
cobalt (II) salts, cotton bleaching 709
COD 17, 537–539, 544, 961, 1001,
1005–1006, 1129–1130
cold alkali extraction 1046
cold alkali purification 934
– efficiency after hot caustic extraction 948
cold aqueous NaOH solution, eucalyptus
prehydrolysis-kraft pulp 943
cold blow technology 274–275
cold caustic extraction 942–952
– NaOH concentration 1046
– pulp purification 935
– temperature dependence 945
cold displacement
– displacement cooking process step 370
– prehydrolysis-kraft process 348–350
cold water extraction 1225
collection rate versus utilization rate, CEPI
countries 1171
collection systems
– efficiency 1180–1181
– recovered paper 1177
color, acid sulfite cooking liquor analysis 433
color reversion 1041
combined-cycle technology, black liquor
gasification 993
commercial lignin 717–718
commercial paper pulp
– chemical characterization 1013–1014
– fiber dimensions 1021
– molecular weight distribution 1019
compact feed system 381–382
compact press, Kvaerner 557
comparative evaluation, sodium ion diffusion
coefficient 149–150
complex acids, hot caustic extract 961
complexometry, operating principle 1221
compression forces
– Norway spruce pulp 1276
– single wet fibers 1275
compression wood 55
compressive dewatering 525–526
– pulp washing theory 517
concentration profile, Kazi and Chornet
diffusion model of impregnation 153
concept of Bouchard 798
condensation
– b-O-4 arylether structures 410
– degradation products with lignin units
420
– lignin 167–168
– sulfite cooking chemistry 414–415
– with phenols 424–425
conditioning 1216
conditions, ozonization 843–849
conducting system, functional elements
46–48
conductivity, acid sulfite cooking liquor
analysis 433
Confederation of European Paper Industries
1157
conical-disc refiners 1105–1106
coniferous woods
– structure 50
– terpenes 35
coniferyl-type structures, formation 170
coniferylaldehyde 342
coniferylaldehyde-type structures, sulfonation
of a-position 412
consistency
– as function of screening zone length 570
– pulp 708
– pulp bleaching 1128
– two-stage delignification operating
conditions 730
construction material compatibility 893
consumer demand, recycled papers 1199
contaminant removal 594–600
– arrangements 596–598
– design principles 594–596
– efficiency 598–599
– selective 592–594
contaminants
– centrifugal cleaning operating parameters
588
– screening operating parameters 579
continuous batch cooking see CBC
continuous cooking
– equipment in comparison to batch
cooking 366
– outline of single-vessel system 377
– principles 377–378
– process steps 378–380
– results 295–306
– technology and equipment 377–391
Index 1303
continuous digester, in conventional chip
feeding system 380
continuous liquor flow
– carbohydrate composition of pulp 255
– comparison with standard batch cooking
245
contoured-drum rotor (S-rotor), pressure pulse
profile 573
convective air movement, pile interior 99
conventional cooking, effective alkali profile
276–277
conventional drum washers, pulp washing
equipment 547–549
conventional heat recovery system 391
conventional kraft pulp
– effect of polysulfide 312
– residual lignin structures 262
– RLCC composition 640–641
conveyor systems, stationary 97–98
cooking
– acid sulfite pulping process chemistry 430
– chemical cycle 973–974, 986
– continuous cooking process step 379
– prehydrolysis-kraft process 348–350
– standard batch 229–234
cooking chemicals
– recovery 968, 994
– selected model of kraft cooking kinetics
217–220
– sulfite chemical pulping 395–403
cooking conditions, influence on acid sulfite
pulping process chemistry 459–465
cooking liquor
– acid sulfite 396
– analysis methods 433
– displacement 430–434
cooking temperature
– decrease in modified kraft cooking
249–250
– effect on modified kraft cooking 248–251
– in relation to kappa number and dissolved