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Handbook of Size Exclusion Chromatography and Related ...

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Ball-milled straw lignin <strong>and</strong> enzymatically isolated lignin have been<br />

extracted from wheat straw <strong>and</strong> from straw residues, respectively (77). The alkali<br />

lignin was obtained by treatment <strong>of</strong> wheat straw with 0.5 MNaOH at 758C. The<br />

effect <strong>of</strong> ball-milling time (BMT) on lignin yield <strong>and</strong> MM was examined. A<br />

comparative study <strong>of</strong> ball-milled lignin, enzyme lignin, <strong>and</strong> alkali lignin using<br />

structural determinations <strong>and</strong> SEC with an alkaline eluent was performed. The<br />

alkali lignin, which was relatively free <strong>of</strong> polysaccharides <strong>and</strong> appeared to have<br />

high MM, had the greatest potential for further investigation.<br />

The effect <strong>of</strong> different hemicellulases on birch kraft pulp was evaluated by<br />

following the amount <strong>of</strong> lignin leached from kraft pulp after enzymatic treatment<br />

(78). An increase in the amount <strong>and</strong> MM, determined by SEC using an alkaline<br />

eluent, <strong>of</strong> the lignin extractedfrom thexylanase-treated pulpswas observedwhen<br />

compared to the lignin extracted from the untreated pulp.<br />

The effect <strong>of</strong> a commmercial xylanase preparation from Trichoderma<br />

longibrachiatum <strong>and</strong> Trichoderma harzianum E58 was tested on kraft pulp (79).<br />

BymonitoringtheMMD<strong>of</strong>untreated<strong>and</strong>treatedpulpsitwasseenthattheMM<strong>of</strong><br />

lignin extracted from enzyme-treated brownstock was much larger than that from<br />

the control pulp.<br />

Theuse<strong>of</strong>ligninsfractionatedaccordingtomolarmassintheinvestigations<br />

<strong>of</strong> effects <strong>of</strong> oxidative enzymes has been presented (80). In this system, alkaline<br />

eluents <strong>and</strong> preparative <strong>and</strong> analytical Superdex columns were used (Fig. 4).<br />

Neutral-detergent fibers <strong>of</strong> cotton stalks was ball-milled for different times<br />

in a porcelain rotary ball mill <strong>and</strong> hydrolyzed by cellulase. The lignin was<br />

extracted by either dioxane:H2O or1M NaOH (81). The effects <strong>of</strong> ball-milling<br />

duration <strong>and</strong> extraction procedure on yield, MMD, <strong>and</strong> carbohydrate content <strong>of</strong><br />

lignin were investigated. The MMD patterns <strong>of</strong> the dioxane lignins were constant,<br />

irrespectively <strong>of</strong> the ball-milling time. It was also seen that the alkali system had<br />

probably extracted lignin molecules <strong>of</strong> larger size since the MM was two to three<br />

times higher than that in the dioxan lignin. The results <strong>of</strong> extractions <strong>of</strong> lignin from<br />

neutral-detergent fiber <strong>of</strong> wheat straw was performed by HP/SEC. The wheat was<br />

ball-milled for 7, 14, 21, <strong>and</strong> 28 days in a rotary ball mill <strong>and</strong> hydrolyzed by a<br />

cellulase for 4 days, <strong>and</strong> the residue was used for lignin extraction by either<br />

dioxane or 1 M NaOH (81). The effects <strong>of</strong> ball-milling time <strong>and</strong> extraction<br />

procedure on lignin yield <strong>and</strong> high-performance SEC features were examined. By<br />

increasing the ball-milling time, an increase in the proportion <strong>of</strong> high MM fraction<br />

was seen. MMD determinations were also used for evaluating how an enzymatic<br />

pretreatment modified the fiber surface. The MMD was studied using 0.5 M NaOH<br />

as eluent, a TSK HW-55S gel, <strong>and</strong> a UV detector. The MMD was determined for<br />

lignins extracted by alkali from the enzymatically treated pulps (83). The treatment<br />

<strong>of</strong> kraft pulp with hemicellulases removes some <strong>of</strong> the xylan <strong>and</strong> renders the fiber<br />

structure more permeable. The increased permeability allows the passage <strong>of</strong> lignin<br />

© 2004 by Marcel Dekker, Inc.

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