Mannonic acid

– content in aldonic acid residues 658

– stabilization of reducing end-groups 657

Mannose

– commercial paper-grade pulp 1013

– concentration development in beechwood

prehydrolysis 337–338

– content as function of H-factor 447

Index

– pulp fraction 440

– spent liquor content as function of

Viscosity 459

Maple, density and void volume 128

Maple chips, storage 99

market situation, pulping processes 8–15

Mass balance

– contaminant removal efficiency 598–599

– screening theory 567

– Visbatch® cook of Eucalyptus urograndis

349–350

Mass reject ratio

– in relation to fractionation index 600

– in relation to screening efficiency 589

Mass transfer

– by diffusion 518

– degree of delignification 697

– kraft cooking 122–163

– oxygen delignification 671–687

– ozone bleaching 798–801

Material balance

– kraft recovery boiler 982–984

– one-stage acid sulfite cooking 458

– prehydrolysis-kraft process 347–351

Mathieson process, chlorine dioxide

Generation 742

MbG see methyl-b-d-glucopyranoside

MC ozone bleaching, ozone charge

Dependence 837

Mc pump, pressurized peroxide bleaching

System 866

MC technology 721

MCC 298

– cellulose DP in relation to pulp yield 256

– global production 11

– process steps and flow regime 385

– pulp bleachability 296

– reaction scheme 1026

– results 295–297

– strength properties of softwood pulp 297

– technology and equipment 383–386