Головна

Section 4.3.5

  1. Residual Lignin Structure (see Section 4.2.5)
  2. SECTION 11. CLAIMS AND COMPLAINTS
  3. SECTION 12. BANKING AND PAYMENTS
  4. SECTION 13. INSURANCE
  5. SECTION 14. TRANSPORTATION AND SHIPPING. PACKING
  6. SECTION 16. REVISION
  7. SECTION 2. SIMPLE COMMERCIAL LETTERS

1Svensson, S., Charging apparatus for

cellulose digesters. SE 86978: Sweden,

1936.

2Vilamo, E., O. Aho, K. Aunio, Pulping

according to Vilamo. Svensk. Papperstidn.,

1955; 58(12): 452-457.

3Yorston, F.H., N. Liebergott, Correlation

of the rate of sulphite pulping with temperature

and pressure. Further studies.

Pulp Paper Mag. Can., 1965: 272-278.

4Goldfinger, G., Variation of the order

and energy of activation of the delignification

reaction in sulphite cooking.

Tappi Section - Paper Trade J., 1941:

289-291.

5Rusten, D., Degradation of cellulose

and solution of hemicelluloses during

spruce sulfite pulping. Norsk. Skogindustri,

1962; 16: 328-339.

6Fischer, K., I. Schmidt, Kinetics of cellulose

and lignin degradation during the

acid bisulfite process and the possibilities

for cooking control. Tappi J., 1991;

74(1): 182-185.

7Haywood, S.T., An empirical cooking

model for magnesium bisulphite pulp.

Pulp Paper Canada, 1989; 90(6):

112-114.

8Yaldez, R., A. Ecker, H-factor determination

for viscosity degradation during

acid sulfite pulping of beech wood.

R&D Lenzing AG: Lenzing, 2000.

9Schelosky, N., T. Baldinger, Determination

of small anionic sulfur species in

magnesium base bisulfite cooking

liquor by capillary electrophoresis (CE).

Lenzinger Ber., 2000; 79: 108-112.

10Kaufmann, Z., Uber die chemischen

Vorgange beim Aufschlu. von Holz

nach dem Sulfitprozess. PhD-Thesis,

ETH: Zurich, 1951.

11Ivancic, A., S.A. Rydholm, Technical

color reactions of lignin. Svensk. Papperstidn.,

1959; 16(62): 554-566.

12Ingruber, O.V., Pulp Paper Mag. Can.,

1954; 55(10): 124-131.

13Promberger, A., Influence of storage

conditions of beech wood on sulfite

pulping processability and final pulp

properties. PhD-Thesis, In Institute of

Pulp, Paper and Fiber Technology. Technical

University: Graz, 2004: 191.

14Sixta, H., Acid magnesium sulfite cooking

of beech and spruce woods. 1:

Course of the degradation of wood components.

R&D Lenzing AG: Lenzing,

2002.

15BeMiller, J.N., Acid-catalyzed hydrolysis

of glycosides. Adv. Carbohydrate Chem.,

1967; 22: 25-108.

16Rohrling, J., et al., A novel method for

the determination of carbonyl groups in

cellulosics by fluorescence labelling. 1.

Method development. Biomacromolecules,

2002; 3(5): 959-968.

17Rohrling, J., et al., A novel method for

the determination of carbonyl groups in

cellulosics by fluorescence labelling. 2.

Validation and applications. Biomacromolecules,

2002; 3(5): 969-975.

18Rohrling, J., et al., Determination of carbonyl

functions in cellulosic substrates.

Lenzinger Ber., 2002; 81: 89-97.

19Potthast, A., et al., A novel method for

the determination of carbonyl groups in

cellulosics by fluorescence labelling. 3.

Monitoring oxidative processes. Biomacromolecules,

2003; 4(3): 743-749.

20Rydholm, S.A., Pulping Processes. Original

edition 1965. New York: Wiley

(Interscience), 1965: 439-576.

21Patt, R., D.L.-K. Wang, Qualitatsbeurteilung

von Chemiezellstoffen. Teil 2:

Alkaliloslichkeit und Gesamtzuckeranalyse.

Das Papier, 1987; 41(1): 7-12.

22Dunlop, A.P., Furfural formation and

behavior. Ind. Eng. Chem., 1948; 40(2):

204-209.

23Harris, J.F., et al., Factors influencing

dilute sulfuric acid prehydrolysis of

southern red oak wood. Prog. Biomass

Conversion, 1984; 5: 101-141.

References 507

24Erdtman, H., The phenolic constituents

of pine heartwood. V. The heartwood of

Pinus strobus. Svensk. Kem. Tid., 1944;

56: 2-14.

25Erdtman, H., The phenolic constituents

of pine heartwood. VIII. Ultraviolet

absorption and steric configuration of

pinosylvin. Svensk. Kem. Tid., 1944; 56:

134-142.

26Erdtman, H., The phenolic constituents

of pine heartwood. VII. The heartwoods

of Pinus nigra Arn, Pinus montana Mill.,

Pinus banksiana Lamb, and Pinus palustris

Mill. Svensk. Kem. Tid., 1944; 56:

95-101.

27Erdtman, H., The phenolic constituents

of pine heartwood. VI. The heartwood

of Pinus cembra L. Svensk. Kem. Tid.,

1944; 56: 26-31.

28Hoge,W.H., Tappi, 1954; 37: 369.

29Mutton, D.B., Hardwood resins. Tappi

J., 1958; 41: 632-643.

30Harris, J.F., Acid hydrolysis and dehydration

reactions for utilizing plant carbohydrates.

Applied Polymer Symp.,

1975; 28: 131-144.

31Conner, A.H., Kinetic modeling of hardwood

prehydrolysis. Part I. Xylan

removal by water prehydrolysis. Wood

Fiber Sci., 1984; 16(2): 268-277.

32Sixta, H., Cellulose preparation and

recycling of raw materials and auxiliaries

by the Lenzinger magnesium

bisulfite process. Lenzinger Ber., 1986;

61: 5-11.

33Rydholm, S., S. Lagergren, On the

delignification reactions of the technical

sulfite cook. Svensk. Papperstidn., 1959;

62(4): 103-122.

34Sixta, H., Acid magnesium sulfite cooking

of beech and spruce woods. 2: Influence

of cooking conditions. R&D

Lenzing AG: Lenzing, 2003.



Section 4.3.4 | Section 4.3.6

Stora Processes (Hydrogen Sulfite or Monosulfite-Acid Sulfite) | Alkaline Sulfite Pulping | Na2SO3 Na2CO3 NaOH | References | Section 4.2.3 | Section 4.2.4 | Section 4.2.5 | Section 4.2.6 | Section 4.2.7 | Section 4.2.8 |

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