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ISSN ………… - International Network for Bamboo and Rattan

ISSN ………… - International Network for Bamboo and Rattan

ISSN ………… - International Network for Bamboo and Rattan

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pressures usually between 4 <strong>and</strong> 8 bar in alkaline medium, per<strong>for</strong>med at high consistencies of 20-30<br />

per cent <strong>and</strong> temperatures of 90-140 0 C, depending on the alkali used. But as it is not a selective<br />

lignin- degrading chemical, pulps cannot be bleached to high brightness exclusively with oxygen<br />

without considerable attack on the polysaccharides, resulting in rather poor strength properties. Thus<br />

the common practice in mill-scale bleaching today is to remove about one–half of the residual lignin<br />

in unbleached pulps by oxygen, <strong>and</strong> to finish with conventional multi stage bleaching sequences such<br />

as C-(EO)-H-D, D-C-(EO)-D, O-C-D-E, O-C-E-D-E-D or O-D-E-D, etc. The conventional bleach<br />

plants employing sequences such as C-E-H-H will have to do only marginal changes in their industry<br />

to incorporate the D-C-(EO)-D process so that pulps of high brightness can be produced at<br />

considerably <strong>and</strong> relatively low cost. The Kamyr, Sund, Beloit Rauma, etc. have equipments <strong>for</strong> the<br />

needful modifications (Goel et al. 1989) 5 . More than 16 plants throughout the world are employing<br />

this process, the first having been founded in South Africa in 1970. The main practical advantage of<br />

oxygen bleaching is the fact that the effluents from the oxygen step can be processed within the<br />

normal kraft recovery system. In the context of increasing air <strong>and</strong> water pollution from the traditional<br />

bleaching systems, oxygen bleaching has proven its potential as the more environmentally friendly<br />

system.<br />

4.3.2. Colour reduction in the effluent<br />

Some of the technological changes as suggested by Mall et al. (1989) 52 , <strong>for</strong> reducing toxicity <strong>and</strong><br />

colour of the effluents are: elimination or minimum use of sulphur containing pulping processes <strong>and</strong><br />

chlorine containing bleaching processes; extended delignification; modification of bleaching<br />

sequences which includes elimination of caustic extraction stage which is the major contributor of<br />

colour; use of oxygen bleaching, chlorine dioxide bleaching; use of anthraquinone <strong>and</strong> lower sulphur<br />

high-yield pulping processes; total recycle concept, <strong>and</strong> reduction in bleached pulp brightness level.<br />

4.3.3. Bio-bleaching<br />

Microorganisms or enzymes can cause modification of the lignin in the pulp rendering it more<br />

accessible to the bleaching agents, thus the application of biotechnology in bleaching can reduce the<br />

consumption of bleaching chemicals which can further help to reduce the effluent pollution <strong>and</strong><br />

associated toxicity problems. After the alkaline extraction stage, unbleached kraft hardwood pulps<br />

have been treated with xylanases of Escherichia coli clone to yield pulps which are bright <strong>and</strong> have a<br />

kappa number 54 per cent lower than the corresponding control samples (Jurasck et al. 1987) 493a . In<br />

addition, the viscosity of pulps was also higher compared to the control. Begasse CTMP <strong>and</strong> CMP<br />

pulps on treatment with a crude enzyme extract resulted in 2-6 unit improvement in brightness<br />

(Ramaswami <strong>and</strong> Ramanathan 1989) 66 . There is still scope to improve its per<strong>for</strong>mance by<br />

purification of the enzyme <strong>and</strong> identification of the optimal treatment conditions like temperature <strong>and</strong><br />

25

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