- •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
Xylose 463
– in relation to pentosan and screened yield
463
– influence on CBC process 289–290
– influence on pulp yield in standard batch
cooking process 231–233
copper number
– commercial paper-grade pulp 1014
– dissolving pulp characterization 1062
– functional groups determination 1235
– unpurified pulp 952
copper number method 441
corn straw fibers, cell dimensions and
chemical composition 4
corona discharge, ozone generation 783
cotton linters
– acetylation 1046
– cell dimensions and chemical
composition 4
– dissolving grade pulp 1022
– low polydispersity 1044
– molar mass distribution 1049
– molecular weight distribution 1035
– representative dissolving pulp 1036
– water-accessible pore volume 1053
cottonwood, average moisture content 125
countercurrent cascade, pulp washing mixing
stages 539
creosol
– chlorine bleaching 746
– ozone reactions 792
– reactions with chlorine dioxide 747
creosol methyl ether, reactions with chlorine
dioxide 748
critical state, chromatography 1254
Cross, Charles F. 7
crude tall oil, kraft pulping 112
crude turpentine, kraft pulping 112
crystalline cellulose 26
crystalline lattice, packing 27
crystalline material
– H-NMR solid-phase spectrum 1261
– X-ray diffractogram 1260
crystallinity 1042, 1257–1265
– degree of 1041, 1258
crystallinity index 1262
– determination 1258–1259
crystallites, dimension 1263–1265
Crystolon, pulp stone 1093
CS chip screen 90
CSF see Canadian Standard Freeness
CTMP see chemithermo mechanical pulp
CTMP refining 1110
CTO see crude tall oil
CUENE 1241
– cellulose molecular weight determination
1240
CUOXAM 1241
– cellulose molecular weight determination
1240
cupram 1025
cuprammonium, dissolving pulp
applications 1025
Cupressus, sesquiterpenic tropolone derivates
35
1304 Index
cupri-ethylene-diamine(-solution) see CUENE
cutting geometry, disc chipper 81
cyanohydrin method, functional groups
determination 1237
1,3-cycloaddition, lignin degradation 790
cyclone parameters, centrifugal cleaning
586–587
cylindrical coordinates, Fick’s second law of
diffusion in 152
cylindrical refiners 1105–1106
cymene, conversion of a-pinene during sulfite
pulping 426
d
D*-stage 764
DAE see differential algebraic equations
Dahl, Carl 5
Dakin-like reaction 858
Darcy’s law 132, 147, 513
DCM, extractive 234, 330, 342, 360, 365,
450–451, 961, 1013, 1030, 1061
deacetylation, glucomannan in superbatch
process 280
debarker, Nicholson A2 78
debarking 71–80
– methods 72–80
debarking resistance, seasonal development
1077
debarking state, wood quality 1075
debris passage ratio, in relation to screening
efficiency 590
Debye–Huckel–Onsager equation 142
decayed wood, waste generation 105
deciduous woods, structure 50
decomposition
– chlorine dioxide 737
– homolytic 651
– hydrogen peroxide 854–856
– metal ion-catalyzed 791
decreasing-permeability model 517
defiberization, lignin compounds 1123
defibration
– conditions 1102
– single fibers 1083
deflocculation, fibers 562
degradation
– carbohydrates 794–798, 859
– cellulose 1056–1059
– cellulose/hemicellulose under alkaline
conditions 175
– end products 956
– lignin 790–794
– pathways for glucosone and xylosone endgroups
659
– pentoses and hexoses 420
– products 446
– wood components 437–449
degradation acids, relative frequencies
(oxidative degradation) 637
dehydration, carbohydrates 419–421
deinking 1165, 1174–1175
deliberation 1113
– single fibers 1083
delignification 16–17, 61, 79, 110–112,
158–162, 705–706, 828–829
– activation energy literature data 201–202
– alkali charge 700
– alternative bleaching methods 887
– as function of pH 473
– beechwood acid sulfite cooking 437
– behaviour 834
– bleaching 809, 887
– blowtank 826
– brightness dependence 870
– carbohydrate reactions 657
– chain scissions number 260
– chlorine dioxide 752, 755
– degree of 697, 717
– dioxygen-alkali delignification processes
657–666
– DualoxTM system 730
– effect of carry-over 717
– effect of impregnation on delgnification
uniformity 158–162
– effect of increasing chlorine dioxide 762
– electrochemical 887
– Eucalyptus saligna prehydrolysis kraft pulp
with oxygen delignification 260
– extent 1228–1229
– final pH 705
– hemicellulose degradation in initial phase
251
– H-factor 259
– high-shear mixers 826
– industrial 688, 695
– kappa number 258, 678, 684
– kinetics 211–215, 671–685
– kraft cooking 184, 189, 211
– lignin solubilization 714
– low-consistency ozone bleaching 809
– mass transfer rate 697
– medium-consistency ozone delignification
system 826
– NaOH-charge 730
– offgas 826