- •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
Index 1343
spinnability, cellulose 1034
spiral burrs, pulp stone 1094
spiral thickenings 44
spruce
– average moisture content 125
– characterization of unbleached kraft pulp in
CBC and conventional cooking 285
– chemical composition 360, 451
– comparison of kraft cooking experiments
with predictions of selected kinetics model
225
– density and void volume 128
– diffusion coefficient 148–149
– kraft cooking selectivity plot 226, 232, 243
– lignin weight fractions 213
– pH, pulp yield and acetyl content 474
– pulp 109
– selectivity plot for different alkali ratios in
AS/AQ pulping 479
– Sivola process pulp properties 469
– stem section 55
– Visbatch® process conditions 365
– viscosity–H-factor relationship 452
spruce CBC pulp 285, 292
spruce sulfite cooks, pulp and spent liquor
compositions 448
spruce sulfite pulp, brightness increase 879
spruce wood, ASAM pulping process 59
SR see Schopper-Riegler method
stabilization, reducing end-groups 657–660
stabilized end-groups, peeling reactions 662
stacker reclaimer, boom-type 103
stages, liquor circulation 888–890
staining methods, fiber identification. 1270
stalk fibers, cell dimensions and chemical
composition 4
standard batch cooking process 229–234
– carbohydrate composition of pulp 255
– parameters 234
standard chlorine dioxide bleaching 754–759
standard grades of recovered paper and board,
European list 1203–1210
standardized Norden efficiency factor
545–546, 558
standardized outlet consistency 545
starch, wood content 30
static mixers, bleaching equipment 621–622
static ozone bleaching 800
stationary conveyor systems, log handling
97–98
Staudinger-Mark-Houwink equation
1250–1251
steam
– generation, kraft recovery boiler 985
– pressurized peroxide bleaching system
867
steam consumption, reduced with cold blow
technology 274
steam drum, kraft recovery boiler 981
steam economy, multiple-effect evaporation
978
steam mixers, atmospheric 622–623
steam pressure, effect on penetration rate
during pre-steaming 130
steaming
– acid sulfite pulping process chemistry 428
– effect on air removal 131
– impregnation 405
– kraft cooking pretreatment 129–132
steel plate conveyor, log handling 98
steeping, dissolving pulp 1026
stem section, Lophira alata 58
stem structure, wood characterization level
21
step rotor, cross section 564
stepwise degradation, effect on molecular
weight 959
steric intramolecular interactions, glycone
327
steroids, hardwoods 37
stilbene
– formation and reactions 411
– relative oxygen susceptibility 640
– softwoods 37
– structure 640
stilbene structures, resistance to chlorine
dioxide oxidation 749
stoker discharger, chip storage 104
Stokes–Einstein model, diffusion 147
Stokes’ law 582
stone groundwood 1087, 1098
– definition 1072
stones, selective removal 593
Stora processes 465, 472–475
storage
– recovered paper 1187–1190
– wood yard 69–71
streams
– around a hydrocyclone 579
– around a screen 563
strength delivery, pulp 256–257
strength F-value 1104
strength properties
– CBC pulp 293–295
– MCC® softwood pulp 297