- •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
1338 Index
– stabilization 657–660
reduction, degree of see DR
reduction efficiency 982
reduction energetics, oxygen 643
reduction products, dioxygen 644
reductive bleaching 1134
refiner mechanical pulp 1098
– definition 1072
refiner plates 1108
– designs 1109
refiner process 1098–1112
refiner types, characteristics 1108
reflectance, sheets 1280
reflectance spectra, hardwood sulfite pulp
611
refractive index, acid sulfite cooking liquor
analysis 433
refractory kappa number 672
regenerated cellulose fibers, production by
Viscose process 7
regenerated fibers 1047
– global production 11
regeneration
– black liquor 112
– cellulose II 27
reject handling, pulp processing 1113–1122
reject rate, screening operating parameters
575
reject ratio, volumetric 568–569, 576
reject refining stage 1121
reject thickening, in relation to volumetric
reject ratio 568–569, 576
– screening theory 566–570
reject treatment 1121–1122
relative hydrolysis rates, methyl-b-pyranosides
and 328
relative oxygen susceptibility, lignin model
compounds 640
reliability, quality control 1215
removal efficiency, fibers 590–591
repeatability, quality control 1215
reprecipitation, xylan 1011
reproducibility, quality control 1215
residual chromophores 1030
residual lignin 174, 704, 856–859, 1033
– composition after cooking and bleaching
634–640
– contents 722
– functional group content 635
– linkage frequencies 638
– modification with peracetic acid 880
– phenolic hydroxyl content 263
– b-O-4-structures content 263
residual lignin-carbohydrate complex see
RLCC
residual lignin structures 173–174, 713–716,
749
– milled wood lignin, conventional and
EMCC® kraft pulp 262
– modified kraft cooking 257–264
residual phase, kraft pulping reactions
overview 184
residual sodium, unidirectional longitudinal
diffusion 139
resin 1030–1033
– black liquor 967
– dissolving pulp characterization 1061
resin acids
– kraft cooking extractives 183
– softwoods 35–36
resin canals, softwoods 52
resin content, wood quality 1075
resin ducts, softwoods 51
resin reduction 960
resin-rich, softwoods and hardwoods 465
resistance to chlorine dioxide oxidation 749
resistant lignin fractions, partial kappa
numbers 724
resonance structures, chlorine dioxide 735
Resource Conservation and Recovery Act, US
legislation 1195
Resource Recycling Facilitation Law, Japanese
legislation 1198
retention time 702–703, 804
– ozone bleaching 802
– temperature, speed 1098
– two-stage delignification operating
conditions 730
rheology, pulp-liquor systems 614–615
ribonic acid, content in aldonic acid residues
658
rice straw fibers, cell dimensions and
chemical composition 4
ring-conjugated structures, hydroxyl radical
adducts 653
ring debarkers 77–80
ring grinder, mechanical pulping 1088
ring-porous hardwoods, Fraxinus excelsior 53
ring-porous woods
– liquid flow 133
– vessels 53
Ritter–Kellner process 6
– sulfite chemical pulping 392
RLCC 634, 666–668
– composition before and after after
bleaching 640–641