- •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
Viscosity 456
furnace 968
– kraft recovery boiler 981
furnish parameters
– centrifugal cleaning 587–588
– screening 578–579
g
G-factor model for viscosity loss 195–197,
356–357
G-layer see gelatinous layer
galactan, relative acid hydrolysis rates 417
galactoglucomannan see GGM
galactose
– commercial paper-grade pulp 1013
– concentration development in beechwood
prehydrolysis 337–338
– content as function of H-factor 447
– pulp fraction 440
gallic acid, structure 425
gas chromatography, monosaccharides
determination 1231
gas management 828
– continuous cooking process step 380
– displacement cooking process step 372
gas phase ozone bleaching 808
gas void fraction 690, 701, 805
– ozone generation 784
gasification 992
– low-temperature 482
gel column, size exclusion characteristics
1255
gel permeation 1252
gel permeation chromatography (GPC)
measurements 181, 255–256, 263, 415,
1237, 1256
– functional groups 1017
– lignosulfonates 415
– measurements 842
gel phase, polymers 1252
gelatinous layer 55
GentleFeed system, debarking 74
geometric progression, finite 541
Index 1313
GGM 186–187, 211, 215–216, 234, 251–252,
283–286, 291–293, 476
– dissolution in CBC process 284
– pulping yields 110–111
– removal in CBC process 286
Girard-P method, functional groups
determination 1237
GL&V Impco HI-Q Knotter 602
glassy state, cellulose bleaching 1042
global production capacity, oxygen-delignified
pulp 631
glucan
– dissolving pulp characterization 1061
– residue 936
glucoisosaccharinate, hot caustic extract 961
glucoisosacharinic acid, black liquor
composition 968
glucomannan 1028
– deacetylation in superbatch process 280
– degradation rate in Gustavson–Al-Dajani
kinetic model 253
– molecular structure 28
– pulping yields 110
– specific consumption in selected model of
kraft cooking kinetics 221
– specific kraft pulping reactions 180
– TCF-bleached dissolving pulp 1049, 1051
– yield as function of lignin yield 481
Gluconacetobacter xylinum 24
gluconic acid
– content in aldonic acid residues 658
– ozonation 796
glucose
– commercial paper-grade pulp 1013
– concentration development in beechwood
prehydrolysis 337–338
– content as function of H-factor 447
– polysaccharide chain cleavage 662
– reactions with sulfonic acid 422
– spent liquor content as function of
Viscosity 459
glucosone end-groups, degradation pathways
659
glucuronic acid, isomerization products 1234
glucuronoxylan, pulping yields 110
d-glyceric acid, polysaccharide chain
cleavage 662
glycolic acid
– black liquor composition 968
– ozone decomposition, initiator 789
– polysaccharide chain cleavage 662
glycone, steric diequatorial intramolecular
Interactions 327
glycosidic bond
– b-elimination 177
– ozonation 830
glycosidic linkages
– alkaline hydrolysis 178
– degradation 859
glyoxylic acid, ozone decomposition, initiator
789
GM see glucomannan
goniometer, X-ray diffractometer 1260
GPC see gel permeation chromatography
graphic papers, utilization rate 1169
grass fibers, cell dimensions and chemical
composition 4
gravimetry, operating principle 1221
gravitational field, earth 582
gravity separators, hydrocyclone 579
gray alder, chemical composition of wood 23
green liquor 112, 117, 243, 394, 986–992,
1004, 1007
– clarified 988
– kraft pulping 112
– Na2
S 241
green wood, average moisture content 125
Greening the Government by Waste
Prevention, Recycling, and Federal
Acquisition, US legislation 1196
grinders, mechanical pulping 1089–1090
grinding
– machines and aggregates 1087–1095
– mechanical and thermal processes
1080–1083
– parameters 1084
– pulping 1079–1098
– zonal temperatures 1082
grits, white liquor preparation processes 989
groundwood
– components 1114
– flow sheet 1088
– properties 1084–1087
Guaiacum officinale, caoutchouc 38
guaiacyl 713
guaiacylglycerol-b-guaiacyl-ether 858
guaiacylpropane
– lignin 165
– molecular structure 32
Gustavson and Al-Dajani kinetic model
– degradation rates for xylan, glucomannan
and HexA 253
– hemicellulose degradation 252
gutta 38
gymnosperms, lignin 30