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IS EXTENDED COOKING NECESSARY FOR THE CLOSURE OF BLEACH PLANT? - A STRATEGIC SHIFT IN PULPING AND BLEACHING

机译:关闭漂白剂是否需要延长烹饪时间? -制浆和漂白的战略转移

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Elemental Chlorine Free (ECF), Totally Chlorine Free (TCF), and Totally Effluent Free (TEF) bleaching of pulps requires low Kappa number pulps to bleach plant. Lowering of kappa number is usually achieved by extended delignification in digesters; reduced yield and increased wood cost per ton of pulp are the consequences. With the increasing cost of wood, the basic premise of extended cooking (EC) to lower the pulp kappa number is questioned. A strategic shift in pulping and bleaching is discussed to decrease wood use per ton of pulp (or more pulp from a ton of wood used) while decreasing the kappa number of pulp to bleach plant. Such a shift would allow the mills to lower bleaching cost, comply with the environmental requirements under Cluster Rules but most importantly, allow the closure of bleach plants cost effectively. The approach involves high kappa pulping and selective delignification of softwood pulps by oxygen before ECF or TCF bleaching. To avoid the loss of yield gained from high kappa pulping to screen rejects, pulping could be carried out using combination of digester additives like anthraquinone (AQ), polysulfide (PS) and surfactant based chip penetrants (SURF). Other benefits include savings in Active Alkali (AA), H-Factor, and decreased solids and heat loads to recovery boiler. Using oxygen, the pulps can be selectively delignified with little loss of yield and strength but with strong resolution of dirt and shives. This approach requires capital investment and some operating costs; attractive cost-benefit is mandated to justify the capital investment. A detailed cost-benefit analysis (CBA) has run to outline the benefits of high Kappa pulping, oxygen delignification and chlorine free bleaching (both ECF and TCF bleaching) to 88-89 %ISO brightness over conventional extended pulping and bleaching. High rate of return on the investment (%ROI) and shorter pay-back on the expended capital do justify this shift in pulping and bleaching.
机译:纸浆的无元素无氯(ECF),完全无氯(TCF)和完全无污水(TEF)漂白要求使用低Kappa值的纸浆漂白植物。降低卡伯值通常是通过在消化池中延长去木质素来实现的。结果就是降低产量和每吨纸浆的木材成本。随着木材成本的增加,人们对延长蒸煮(EC)降低纸浆卡伯值的基本前提提出了质疑。讨论了制浆和漂白的战略性转变,以减少每吨纸浆的木材使用量(或从使用的一吨木材中提取更多的纸浆),同时减少到漂白厂的纸浆的卡伯值。这种转变将使造纸厂降低漂白成本,符合《集群规则》中的环境要求,但最重要的是,可以经济有效地关闭漂白厂。该方法涉及在ECF或TCF漂白之前,用高Kappa制浆和通过氧气对软木纸浆进行选择性脱木素处理。为了避免从高卡伯制浆到筛分废品而导致的产量损失,可以结合使用诸如蒽醌(AQ),多硫化物(PS)和基于表面活性剂的切屑渗透剂(SURF)之类的蒸煮添加剂来制浆。其他好处包括节省了活性碱(AA),H因子,并减少了固体和减少了回收锅炉的热负荷。使用氧气,可以选择性地对纸浆进行脱木质素处理,收率和强度的损失很小,但污垢和碎屑的分离力却很强。这种方法需要资本投资和一些运营成本;强制要求有吸引力的成本效益来证明资本投资的合理性。详细的成本效益分析(CBA)概述了高Kappa制浆,氧脱木素和无氯漂白(包括ECF和TCF漂白)与传统的扩展制浆和漂白相比达到88-89%ISO亮度的好处。高投资回报率(%ROI)和较短的投资回报期确实证明了制浆和漂白这一转变的合理性。

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