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6 Wood Discoloration

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248 9 Positive Effects of <strong>Wood</strong>-Inhabiting Microorganisms<br />

tannophilus. Other fungi, e.g., molds, as well as aerobic and/or anaerobic bacteria<br />

can produce amino acids, antibiotics, enzymes, organic acids, solvents,<br />

and vitamins from glucose or glucose-containing wastes. Technical problems<br />

of acid hydrolysis, such as corrosion of the reaction vessels and formation of<br />

noxious by-products, led to research on enzymatic hydrolysis processes, which<br />

promised, for example, higher sugar yields (Saddler and Gregg 1998).<br />

Spent sulphite liquors contain at about 50% of the employed wood as lignin<br />

sulphonic acids and simple sugars from the hemicelluloses. A number of applications<br />

for lignosulphonates or the entire spent sulphite liquors have been<br />

developed in the past (e.g., Faix 1992). Since the early past century, the hexoses<br />

in spent softwood liquors were converted by yeasts to alcohol and the pentoses<br />

in hardwood liquors to fodder or feeding yeast, respectively. For example, a mill<br />

in Switzerland produced (in 1980) in two tanks (320 m 3 ) 82,000 hL alcohol and<br />

7,000 t of yeast cells, respectively. In Sweden, 1.2 million hL of alcohol was produced<br />

in 33 plants in 1945 (Herrick and Hergert 1977). In the 1980s, the sugars<br />

in spent sulphite liquor were converted by means of the soft-rot deuteromycete<br />

Paecilomyces variotii for use as animal feed in Finland (“Pekilo-process”; Forss<br />

et al. 1986). Han et al. (1976) cultured Aureobasidium pullulans on straw hydrolysate<br />

for production of single cell protein. Ek and Eriksson (1980) used<br />

Sporotrichum pulverulentum for water purification and protein production.<br />

Anaerobic treatment of pulp mill effluents by bacteria was reviewed by Guiot<br />

and Frigon (1998).<br />

9.6<br />

Grinding and Steam Explosion<br />

Among the physical pretreatment methods, grinding of lignocelluloses increases<br />

the inner surfaces of the wood cell wall and thus improves the accessibility<br />

for enzymes to the cell wall components. The particle size must be<br />

reduced to 50µm to maximize the effect. The energy costs become prohibitive<br />

at particle sizes of 200µm (Dart and Betts 1991).<br />

Steam explosion methods saturate the lignocellulose with steam and then<br />

allow it to undergo explosive decompression. The treatment releases acids<br />

that contribute to the disruption of the cell wall (Dart and Betts 1991). In the<br />

steaming-extraction process, chopped wood was treated in watery or alkaline<br />

solution for a few minutes at 185–190 ◦ C (1,100–1,200 kPa). Subsequent washing<br />

with water or thin sodium hydroxide solution separated the wood into<br />

a solid component containing lignin and cellulose and a liquid phase of the<br />

hemicelluloses (Dietrichs et al. 1978). In vivo digestibility of wood in a test<br />

cow increased from about 5% of natural wood to 80% for steam-treated wood<br />

(Puls et al. 1983). The hemicellulose fraction was used to produce Paecilomyces<br />

variotii mycelium and enzymes (Schmidt et al. 1979).<br />

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