- •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
1326 Index
moisture 1205, 1219
– green wood 125
– grinding process parameters 1084
– wood 124, 1085
molar fraction, ozone 779
molar mass 1034–1037
– average values 1241–1243
– determination 1243–1246
– distribution 951, 1018, 1049
– polymerization 1239
molecular weight 1058
– dependence on bleaching stage 844
molecular weight distribution 951–952, 1251
– bleached commercial paper pulp 1019
– b-cellulose 443
– dissolving pulp 1034
– wood dissolving pulp 1035
molybdovanadophosphate heteropolyanions,
alternative bleaching methods 887
monolignol
– lignin 31
– structural units 31
monomeric sugars, concentration
development in beechwood prehydrolysis
339
monomodal distribution, molecular 933
monosaccharides
– after hydrolysis 1231–1232
– in water prehydrolyzate from beechwood
340
monosulfite-acid sulfite Stora process
472–475
monoterpenes, softwoods 35
Monterey pine, chemical composition of
wood 23
morphological characterization, pulp fibers
1269
morphology, wood 41–48
MOW see mixed office waste
MOXYprocess 307, 313
– white liquor oxidation 311
MSW see municipal solid waste
multiconical refiner 1107
multiple-effect evaporation 977–979
– principles 977
multistage kraft pulping 325–365
multistage washing 526–527
municipal solid waste 1181–1182
Munk see Kubelka-Munk theory
n
Na-cellulose 1045
– lattice transition 941, 1043, 1045
(Na2S4), polysulfide liquor 306
Na(trium) see sodium
nano-structure, fibers 59–61
NaOH
– charge 730, 953–957
– concentration profile 154–155, 942–944
– dosage in cold caustic extraction 945
– efficiency of chlorine dioxide 768
– initial charge 480
– titrator base 399
native diaryl ether structures 749
native fibers 1047
NCG see noncondensable gases
negative sorting, recovered paper 1188
Nernst equation 309
net heating value 968
neutral magnefite process, two-stage
467–468
neutral sugars, b-cellulose fraction 939
neutral sulfite-acid sulfite process 468–469
neutral sulfite pulping 412–414
– pH range 393
neutral sulfite semi-chemical process see
NSSC
neutralization 872
– black liquor 121
– prehydrolysis-kraft process 348–350
– white liquor 119
Newtonian liquid, laminar flow 1248
Newton’s law, terminal settling velocity 582
Nicholson A2/A8 Debarker 78–79
nitric acid, ozone generation 783
nitrocellulose, dissolving pulp applications
1026
nitrogen adsorption method, specific surface
of dry fibers 1267
NMNO, cellulose molecular weight
determination 1240
NMR spectroscopy 31, 168, 173–174
– solid-phase 1261–1262
– xylan 254
nonaromatic compounds, adsorbable organic
compounds 771
noncellulosic material 933
– carbohydrates 1026
noncondensable gases, falling film
evaporator 975
nonfreezing bound water 1053
nonpaper components, contained in recovered
paper 1204
nonphenolic compound, ozone reactions 790
nonphenolic lignin units 170–172
– structure 171
Index 1327
nonrecoverable paper 1186
– germany 1185
– world 1183
nonuniformity-index see index of
nonuniformity
nonwood plant fibers, economic potential 13
nonwood pulp fiber, global production 9
Norden efficiency (E) factor
– definition 542
– pulp washing 539–546
– standardized 558
North America, recovered paper grades 1161
northern red oak, average moisture content
125
Norway spruce, chemical composition of
wood 23
Noss RadicIone AM 606
Noss Radiscreen 603–604
Noss Raditrim 604
NS-AS see neutral sulfite-acid sulfite process
NSSC 1009, 1110
– role in global pulp production 12
nuclei growth, Avrami-Erofeev’s concept 679
nucleophiles
– addition in kraft pulping reactions 167
– addition of water, chlorine bleaching 747
– lignin attack 648, 856
nucleophilic opening, oxiran 171
nucleophilic reactions, (di)oxygen and
derivatives 647–649
numbering system, European list of standard
grades of recovered paper and board 1205
numerical solution
– cooking chemical concentration equations