- •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 1341
side relief, acid sulfite pulping process
chemistry 429
silo reclaimer, chip storage 102
silo storage, chips 101
silo-stored hardwood chips, Acer saccharum
99
silver birch, chemical composition of wood
23
silver maple, average moisture content 125
simple pit, softwood fibers 123
single-disc refiner 1105
single electron transfer
– degradation mechanism 320
– hydrogen peroxide reactions 852
single elements, determination 1221–1224
single fibers
– cell dimensions and chemical
composition 4
– defibration 1083
– flexibility 1276
– properties 1275–1278
– stress-strain curves 1012
– suspended 1272
single log layer chipping 82
single O2–excited state 645–646
single-phase model, crystallinity 1258
single pulp fibers, stress-strain
characteristics 1277
single-stage oxygen deligniflcation system,
process flowsheet 732
single-vessel continuous cooking system,
outline 377
single-vessel hydraulic digester
– downflow 390
– EMCC®/ITC 386
– Lo-Solids™ process 388
– MCC 383
single wet fibers, parameters 1275
sisal, cell dimensions and chemical
composition 4
Sitka spruce, average moisture content 125
b-sitosterol 37
Sivola processes 468–471
– aspen cooks 468
size-exclusion chromatography 1252, 1254
– water prehydrolyzate from beechwood 340
slaked lime 986
slaker 989
slaking 987–988
slash pine, sorbed sodium–pH relation 520
slewing screw reclaimer, chip storage 103
sludge 1004
– wastewater treatment 1007
smelt 982, 986
– calculation 983
– kraft recovery boiler 985
– sodium carbonate 987
smelt dissolving 988
– weak wash 990
SO2 see sulfur dioxide
soap skimming 967
– displacement cooking process step 371
soda-AQ 178, 194–195, 201–202, 211, 321,
345
– effects on Eucalyptus grandis pulping 325
– see also AQ
soda boiler 962
soda pulping process, discovery 6
sodium
– comparative evaluation of diffusion
coefficients 149–150
– distribution between fiber wall and external
solution 419
– effect on kraft cooking kinetics models
207
– sorption as function of pH 520
sodium-based two-stage sulfite pulping, pHdependency
of delignification, pulp yield
and acetyl content 473–474
sodium borohydride
– cellulose protecting additive 819
– decomposition by hydrogen gas 1236
– post-treatment 822–824
– pulp bleaching 1125
sodium carbonate 987
– conversion 986
sodium chlorate, reduction 741
sodium dithionite, commercial grades 1125
sodium hydroxide 987
– concentration 703
sodium peroxide, industrial bleaching 849
sodium silicate stabilization, pulp bleaching
1129
softening, fibers 1080–1083
softwood fibers
– cell dimensions and chemical
composition 4
– heterogeneity 123
softwood kraft pulp
– comparison of different cooking
conditions 234
– oxygen delignification 713, 723
– selectivity 838
– TCF bleaching with peracetic acid 882
1342 Index
softwood kraft pulping, interdependence of
temperature, cooking time and effective
alkali 251
softwood PHK, representative dissolving
pulp 1036
softwood sawmills, profiling line 88
softwood structure 50–54
softwood-sulfite dissolving pulp 1036
– R18 content 955
softwood xylan, structural changes 252–256
softwoods
– accessory compounds 35–37
– annual ring 51
– axial parenchyma 51
– bleaching 882, 1126
– bordered pits 123
– cellulose 22
– chemical composition of wood 23
– chip pile dimensions 99
– chipper canter 88
– defibration conditions 1102
– diterpenes 35
– fats and fatty acids 36
– flavonoids 37
– hemicellulose 22
– lignans 37
– lignin 22
– lignins 33
– macromolecular substances 22
– monoterpenes 35
– oleoresin 35
– penetrability 135
– phenolic compounds 37
– pits 46, 123
– pulp 1010
– pulp bleaching 1126
– rays 51
– resin acids 35–36
– resin canals 52
– resin ducts 51
– resin-rich 465
– sesquiterpenic tropolone derivates 35
– stilbene 37
– tall oil 36
– tracheids 51
– tropolone derivates 35
– waxes 36
– xylan 29, 252–256
soil-contaminated, waste generation 105
solid-phase NMR spectroscopy 1261–1262
solid-solid separation, liquid environment
562
solid-state NMR spectroscopy 168
solid waste 1006
– municipal 1181–1182
solids concentration, thick liquor 974
solubility
– alkali 1229
– ozone 780–781
– pulp constituents 937
solubility of oxygen, equilibrium conditions
692
solubilization, ozone 802
soluble fraction, alkali solubility tests 1060
solution viscosity 1248–1251
Solvay process, chlorine dioxide generation
742
solvent retention 1268
solvents, cellulose 1240–1241
sootblowing steam, kraft recovery boiler 985
sorbed manganese, as function of pH 523
sorbed sodium, as function of pH 520
sorption, pulp washing theory 519–523
sorted recovered paper, handling 1189
sorting, recovered paper 1187–1190
southem pine, effect of polysulfide 312
southern mixed hartwood, pulp yield as
function of kappa number 230
southern pine, pulp yield as function of kappa
number 230
southern red oak, average moisture content
125
specialty papers, utilization rate 1169
specific consumption, active kraft cooking
chemicals 221
specific drainage resistance 515
specific light absorption coefficient
– residual softwood lignin 266
– unbleached pine 269
specific surface
– as function of fiber concentration 514
– dry fibers 1267
specific volume, pulp bleaching 1131
specific yield loss 949
spectroscopy
– cellular UV 44
– energy dispersive X-ray spectroscopy 40
– Fourier transmission infra-red 159
– NMR 31, 168, 173–174, 254
– Raman 117, 178
– solid-phase NMR spectroscopy 1261–1262
– time-of-flight secondary ion mass
spectroscopy 60
– X-ray photoelectron spectroscopy 60
spent sulfite liquor 448, 962
spermatophytes, lignin 30