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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
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
– 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
Дата публикования: 2015-01-23; Прочитано: 332 | Нарушение авторского права страницы | Мы поможем в написании вашей работы!
