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Involve steeping of the pulp in aqueous solutions of high NaOH concentration
(18–25 wt.%), followed by the addition of appropriate chemicals for subsequent
Derivatization (e.g., CS2 for xanthation or alkylhalides for cellulose ethers). The
Acidic esterification processes yield cellulose nitrate and cellulose acetate. The latter,
More important, conversion process involves a pretreatment with acetic acid
Prior to esterification to triacetate on the addition of acetic anhydride and a catalyst,
Usually sulfuric acid. In a second step, the triacetate is hydrolyzed to the socalled
Secondary acetate (DS between 1.8 and 2.5) on dilution with water and precipitation
Of the flakes. These are then dissolved in acetone to a spinning dope
(polymer concentration above 30%) from which fibers (e.g., filter tow, textile filaments),
Lacquers or plastic are processed.
Since the commercialization of the Lyocell process in 1992, the direct solution
Of pulp in an organic solvent without the formation of an intermediate cellulose
Derivative represents a new processing route for dissolving pulp comprising challenging
demands on pulp quality [10–12].
Dissolving Grade Pulp
For over 80 years, regenerated fibers of high quality and special uses have also
Been spun from a cuprammonium solution (cupram), a metal complex solvent for
cellulose. Less than 2% is estimated for cuprammonium rayon within the world
Rayon production. The high demand on processability and pulp quality requires
The use of high-purity cotton linters which, compared to the viscose process, is not
A decisive cost factor.
Table 11.5 provides a rough overview of the raw material sources, dissolving
Pulp technologies and main applications.
Tab. 11.5 Overview of different applications of dissolving pulps.
Product Simplified reaction scheme Raw material Pulping
Processes
Bleaching
Processes
Viscose
Staple CellOH _I_ NaOH__CellONa B, E, S, H, P*) AS, PHK ECF, TCF
Textile filaments CellONa _ CS2 _ Cell_OCSSNa_0_4_0_5 E, S, H, P*) AS, PHK ECF, TCF
Technical Filament H__Zn2__Na_ __CellOH _II_ P*),MHWPHK (CCE) ECF
Cuprammonium
Rayon
CellOH _I_ Cu__NH3 _4 _OH_2_ __CellOH _II_ CL,S SO, AS ECF
Lyocell
Textile CellOH _I_ NMMO _H2O __CellOH _II_ E, P*), H AS, PHK TCF, ECF
Non-Wovens B, E, S, H, P*) AS, (PHK), K TCF, ECF
Ethers
MC CellONa _ CH3Cl _ Cell_OCH3_x S, E, P, H, MHW,CL AS, (PHK), SO ECF
MHPC CellONa _ CH3Cl PO__
Cell__OCH2CHOCH3_x_OCH3_y_
S, E, P, H, MHW,CL AS, (PHK), SO ECF
HEC CellOH _ EO OH_ __
Cell__OCH2CH2O_x_CH2CH2O_y_
S, E, P, H, MHW,CL AS, (PHK), SO ECF
CMC CellONa _ ClCH2COO_ _
Cell__OCH2COONa_x
S, E, P, H, MHW,CL AS, (PHK), SO ECF
Pulp Properties and Applications
Tab. 11.5 Continued.
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Chemical composition | | | Product Simplified reaction scheme Raw material Pulping |