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In any chemical pulping process, it is essential to achieve adequate penetration of
liquids into the wood. The uniform distribution of the active cooking chemicals
within the chip void system is an important prerequisite for the production of
high-quality pulps, leaving no unreacted zones. Ideally, each fiber in a wood chip
that is being pulped should receive the same chemical treatment which involves
immersion in a pulping liquor of the same concentration, at the same temperature,
and for the same time.
Alkaline pulping is carried out at temperatures in the range between 140 and
175 °C. Under these conditions, the degradation reactions of wood components
are clearly diffusion-controlled. This includes the diffusion of reactants into the
fiber wall and the reaction products out of the chips into the bulk liquor. With a
homogeneous distribution of reagents, the kinetics of the pulping reactions will
also be uniform throughout the system. At low temperatures, the process is no
longer diffusion-controlled, and a reaction gradient is established inside the chip,
so that reaction occurs in all parts of the chip assuring the homogeneous degradation
of wood components. The key procedure to achieve an even distribution of
cooking chemicals prior to pulping reactions is denoted as the “impregnation process”.
The impregnation of wood corresponds to the liquid and chemical transport
into the porous structure of the wood which is characterized by two main mechanisms,
namely: (a) penetration into the capillaries; and (b) diffusion through cell
walls, pit membranes and interfaces. Impregnation of wood is influenced by both
wood properties such as wood species, chip dimensions, moisture content, air
content and the capillary structure as well as the liquid properties such as pH and
chemical concentration, surface tension, viscosity, temperature, and pressure [1].
The quality of impregnation relies on the homogeneity of the chemical treatment
which, in turn, has an impact on the rejects content of the pulp and on the final
product quality.
Penetration refers to the flow of liquid and associated chemicals into the airfilled
voids of the wood chips under the influence of hydrostatic pressure. Penetration
is the process where liquid transfers into the gas- or steam-filled cavities of
the chips. Distinction can be made between forced penetration, including gas and
liquid flow by an externally applied pressure differential, and natural penetration
consisting of capillary rise. Mass transfer stops as the liquid approaches the wood
capillaries that are at the fiber saturation point or that contain liquid–air interfaces.
Hydrostatic pressurization of the system reduces the size of the air bubbles
somewhat, but the effect is small, since extremely high system pressures would
be required to overcome the resistance of the surface-tension forces of multiple
liquid–air interfaces in the narrow capillaries. Under these conditions, entrapped
air dissolves into water to some extent and also can gradually diffuse out of the
pores, while the liquid diffuses into the pores countercurrently.
4.2 Kraft Pulping Processes
The second mechanism, diffusion, is a comparatively slow process and refers to
the diffusion of ions or other soluble matter through the water layer of the cell
wall and pit membrane structure under the influence of a concentration gradient.
Molecular diffusion replaces the reactant chemicals as they are consumed by the
chemical reactions within the chip. All transfer of new chemicals into chips and dissolvedmatter
fromthe chipswill occur through diffusion only after complete penetration.
Thus, molecular diffusion is a very important step in chemical pulping.
Industrial chips are not homogeneous in dimensions and void structure. Moreover,
wood chips – even fromfresh wood – contain air in the void system which must
be displaced as far as possible prior to impregnation to ensure that all parts of the
wood chips can be filled with liquid during penetration. Air removal can be accomplished
by presteaming the chips. Part of the air inside the chips is removed due to
direct expansion by heating, whereas a more complete air removal requires a successive
steam condensation and evaporation in the capillary system of the chips.
In the following sections, the most decisive parameters determining the efficiency
of the impregnation step, such as the heterogeneity of wood structure, presteaming,
penetration and diffusion, will be introduced and discussed.
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