- •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 1317
hydrogen sulfide ion
– concentration in selected model of kraft
cooking kinetics 217–220
– effect on kraft cooking kinetics models
203–206
– effect on modified kraft cooking 241–244
– molar concentration in white liquor 115
hydrogen sulfite
– concentration in cooking liquor 400–401
– Stora process 472–475
hydrogen sulfite ion
– in relation to H-factor 460
– in relation to kappa number and dissolved
Xylose 461
– in relation to screened yield and xylan 462
hydrolysis
– acid-catalyzed 341
– alkaline 178
– hemicelluloses 325–326
– hot acid 883–885
– lignin 407–414
hydrolyzation, fatty acid esters 427
hydroperoxide anions 857
hydroperoxides 645–652, 655–658, 855–859
– formation by enolic structures
autoxidation 651
– formation by phenolic structures
autoxidation 652
– formation in alkaline media 650
– formation, lignin 856
hydroperoxy anions
– concentration 854
– formation 651–652
– ozone decomposition, initiator 789
hydroperoxy radical
– hydrogen peroxide intermediates 852
– ozone decomposition 789
hydrostatic pressurization, impregnation 405
hydrosulfite see dithionite
hydrotrioxide hemiorthoester, ozonation 796
hydroxide ion
– concentration in selected model of kraft
cooking kinetics 217–220
– during VisCBC hardwood cooking process
347
– effect on CBC process 287–289
– effect on cellulose chain scissions 195
– effect on kraft cooking kinetics models
203–206
– effect on modified kraft cooking 237–241
– in relation to pine total pulp yield 240
– molar concentration in white liquor 115
– ozone decomposition, initiator 789
(4-hydroxy-3-methoxyphenyl)-glyoxylic acid,
structure 308
hydroxy acids, hot caustic extract 961
hydroxy carboxylic acids monitoring, role in
H-factor control 191–193
2-hydroxybutanoic acid, black liquor
composition 968
hydroxycarbonic acids, low molecular-weight
961
hydroxycyclohexadienyl radicals, formation
652
a-hydroxyl, structure and relative oxygen
susceptibility 640
hydroxyl groups
– aliphatic 261
– exchange 1102
– phenolic 173
hydroxyl radical 647, 794
– cellulose degradation 859
– during bleaching 777
– formation 712
– hydrogen peroxide intermediates 852
– methanol 788
– phenoxyl radical formation 650
hydroxyl radical adducts
– disproportionation 653
– phenolic coupling 654
– reactions 653–654
hydroxymethylfurfural, formation 419
p-hydroxyphenyl, monolignol structural
units 31
p-hydroxyphenyl groups, resistant lignin 714
p-hydroxyphenylpropane units
– lignin 165
– molecular structure 32
– wheat straw 209
a-hydroxysulfonates, formation 423
hygiene papers, utilization rate 1168
hypochlorite
– consumption 831
– oxidation capacity (OXE) 613
hypochlorous acid 737
– excess 739
i
+I-effect, lignin degradation 790
image analysis, pulp 1274
Impco HI-Q Fine Screen 601
Impco HI-Q Knotter, GL&V 602
impregnation 208–209
– acid sulfite pulping process chemistry 428
– axial 154
– continuous cooking process step 378
1318 Index
– displacement cooking process step 369
– effect on delgnification uniformity
158–162
– Kazi and Chornet diffusion model
151–158
– kraft cooking mass transfer 122–123
– lignin mass balance of Eucalyptus globulus
162
– radial 155
– refiner process 1103
– sulfite chemical pulping 403–405
– two-vessel MCC® system 385
impurities, pulp 708
in-digester washing 557–558
in-situcau sticization 992
incineration
– pulp sample 1220
– single elements determination 1221
index of nonuniformity 1241–1242, 1251
industrial oxygen delignification
– base case parameters 695
– prediction model 688–701
infeed rings, debarkers 79
inhibitors
– ozone 788
– ozone generation 788
initial NaOH charge, in relation to kappa
number and selectivity 480
initial phase
– chlorine dioxide selectivity 761
– kraft pulping reactions overview 183–184
initiators, ozone generation 788
inorganic compounds 1033–1037
– black liquor composition 968
– cellulose protection/degradation 668–671
– commercial paper-grade pulp 1014
– pulp 1219–1224
– woods 39–41
inorganic reactions, kraft pulping 184–185
integral level, wood characterization 21
intercellular layer, cell components 44
interstage washing 948
intra-stage circulation, liquor 888–890
intramolecular formation, epoxides 171
intramolecular hydrogen bond, cleavage 941
intrinsic viscosity 1250
– as function of H-factor 357
– as function of P-factor 353
– as function of residual EA 270, 272, 302
– CED 451
– in relation to pulp strength for kraft
softwood pulp 236
inverse size-exclusion chromatography 1053
ion diffusion, effect of pressure steaming 149
ionic strength
– effect on kraft cooking kinetics models
207
– effect on modified kraft cooking 244–248
iron, removal 862
iron (III) salts, cotton bleaching 709
iron sodium tartrate 1241
irregular piles, wood log storage 1076
ISEC see inverse size-exclusion
chromatography
ISO Standard method
– brightness measurement 610
– see also brightness
isoflavones, hardwoods 38
isoprene units, terpenes 35
isotherm, Langmuir 519
isothermal cooking see ITC
ITC 9, 269–274, 297, 695
– brightness gain in relation to consumed
OXE 273
– process steps and flow regime 387
– single-vessel hydraulic digester 386
– technology and equipment 386–388
j
jack pine, carbohydrate composition of sulfite
and kraft pulp 470
Japan
– legislation 1198
– recovered paper grades 1161, 1163
Jetmixer, Kvaerner 621
Juniperus, sesquiterpenic tropolone derivates
35
Juniperus communis, chemical composition of
wood 23
jute fibers, cell dimensions and chemical
composition 4
juvenile wood 56–59
k
Ka,1, temperature dependence for SO2 397
Kadant Black Clawson Chemi-Washer
551–552
kappa, efficiency of chlorine dioxide 768
kappa factor 755
– efficiency of chlorine dioxide 768
kappa number 17, 111, 137, 190–193,
208–211, 229–245, 249–275, 278–298,
301–305, 312–316, 322–325, 351, 354–357,
363–365, 475–482, 529, 715, 727, 755, 868,
1033, 1228
– as function of alkali ratio in spruce AS/AQ
pulping 479