In conventional kraft cooking 232

– at different digester locations 300

– calculated consumption in Visbatch® cook

Of Eucalyptus urograndis 351

– CBC process 283

– in relation to brightness 272

– in relation to H-factor after 120 min

Cooking 238

– in relation to intrinsic viscosity 270

– in relation to light absorption coefficient

– in relation to pine total pulp yield 239

– in relation to xylan content in unbleached

Visbatch® pulp 358

– influence on pulp yield in standard batch

Cooking process 229

– kraft cooking active chemicals 114–115,

118–119, 159–161

– Lo-Solids™ laboratory cooks 301–303, 305

– predicted concentration in selected kraft

Cooking kinetics model 223, 227

– white liquors 244

Effective capillary cross-sectional area see

ECCSA

Effective filtration pressure, in relation to

Relative pressure washer capacity 536

Efficiency 765

– chlorine dioxide 768–769

– fractionation 590–592

– ozone treatment 829–840

– pulp washing 531, 537–546

Efficiency factor (E factor)

– determination 544

– modified 545–546

– Norden 539–544

Effluent

– biological treatment 999

– pulping processes 998

– treatment 1004–1005

Effluent-free mill 1007

Effluent load

– avoiding 999

– mechanical pulp 1138

– temperature effect 865

Effluent volume, open bleaching stage 892

Einstein see Stokes–Einstein model

Electrochemical delignification, alternative

Bleaching methods 887

Electron density distribution

– benzylium cation 409

– carbonium-oxonium ion 417

– phenylpropene unit 2 633