![]() |
Ãëàâíàÿ Ñëó÷àéíàÿ ñòðàíèöà Êîíòàêòû | Ìû ïîìîæåì â íàïèñàíèè âàøåé ðàáîòû! | |
|
|
– equipment in comparison to batch
Cooking 366
– outline of single-vessel system 377
– principles 377–378
– process steps 378–380
– results 295–306
– technology and equipment 377–391
Index 1303
Continuous digester, in conventional chip
Feeding system 380
Continuous liquor flow
– carbohydrate composition of pulp 255
– comparison with standard batch cooking
Contoured-drum rotor (S-rotor), pressure pulse
Profile 573
Convective air movement, pile interior 99
Conventional cooking, effective alkali profile
276–277
Conventional drum washers, pulp washing
equipment 547–549
Conventional heat recovery system 391
Conventional kraft pulp
– effect of polysulfide 312
– residual lignin structures 262
– RLCC composition 640–641
conveyor systems, stationary 97–98
Cooking
– acid sulfite pulping process chemistry 430
– chemical cycle 973–974, 986
– continuous cooking process step 379
– prehydrolysis-kraft process 348–350
– standard batch 229–234
Cooking chemicals
– recovery 968, 994
– selected model of kraft cooking kinetics
217–220
– sulfite chemical pulping 395–403
Cooking conditions, influence on acid sulfite
pulping process chemistry 459–465
Cooking liquor
– acid sulfite 396
– analysis methods 433
– displacement 430–434
Cooking temperature
– decrease in modified kraft cooking
249–250
– effect on modified kraft cooking 248–251
– in relation to kappa number and dissolved
Äàòà ïóáëèêîâàíèÿ: 2015-01-23; Ïðî÷èòàíî: 338 | Íàðóøåíèå àâòîðñêîãî ïðàâà ñòðàíèöû | Ìû ïîìîæåì â íàïèñàíèè âàøåé ðàáîòû!
