首页> 外文会议>2002 International Pulp Bleaching Conference May 19-23, 2002 Portland, Oregon >PRACTICAL EXPERIENCES IN REDUCING THE ECF BLEACHING COSTS OF AN OXYGEN DELIGNIFIED FULLY-BLEACHED SOFTWOOD KRAFT PULP
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PRACTICAL EXPERIENCES IN REDUCING THE ECF BLEACHING COSTS OF AN OXYGEN DELIGNIFIED FULLY-BLEACHED SOFTWOOD KRAFT PULP

机译:减少氧气脱胶全漂白牛皮纸浆的ECF漂白成本的实践经验

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Pope & Talbot, Inc. produces fully-bleached softwood market kraft pulp at Halsey, OR using an ECF bleaching sequence. Brownstock cooked in continuous digesters utilizing either wood chips or sawdust as their feedstock is processed after washing through a medium consistency, single-stage oxygen delignification system and enters the bleach plant having a 16-20 Kappa number. Since October, 2000 the mill has successfully started-up and optimized a new bleaching sequence including multiple stages of chlorine dioxide (ClO_2) and hydrogen peroxide (H_2O_2), replacing multiple stages of stabilized hypochlorous acid (Monox L) utilized prior to October, 2000. The new bleaching sequence was required to meet Cluster Rule regulations related to AOX and chloroform. After initial startup, laboratory and production trials were completed to reduce ECF bleaching costs without sacrificing pulp quality. Improvements included rebalancing ClO_2 between the D_0, D_1 and D_2 stages, lowering the lignin content of pulp from the (EOP) stage by optimizing H_2O_2 application, operating temperature/pressure and control of metal ions into the stage and reducing demand for ClO_2 at the D_1 stage by improving washing and hence reducing soda carryover from the (EOP) stage washer and better controlling inlet pH. As well, it was found that a pitch fixant being added on bleached pulp was bonding darker fines from pulp machine Whitewater to the fiber and limiting the final brightness of pulp achievable. This issue was resolved by applying talc to properly disperse pitch.
机译:Pope&Talbot,Inc.使用ECF漂白程序在俄勒冈州哈尔西生产完全漂白的针叶木牛皮纸浆。用木片或锯末作为原料的连续蒸煮炉中煮过的黑毛经过洗涤后,通过中等浓稠度的单级氧脱木素系统处理,并进入具有16-20 Kappa值的漂白设备。自2000年10月以来,该工厂已成功启动并优化了新的漂白程序,包括多阶段的二氧化氯(ClO_2)和过氧化氢(H_2O_2),取代了2000年10月之前使用的多阶段的稳定次氯酸(Monox L)需要新的漂白程序才能满足与AOX和氯仿有关的“簇规则”规定。最初启动后,已完成实验室和生产试验,以减少ECF漂白成本,同时又不影响纸浆质量。改进措施包括在D_0,D_1和D_2阶段之间重新平衡ClO_2,通过优化H_2O_2的应用来降低(EOP)阶段的纸浆中木质素含量,操作温度/压力和进入该阶段的金属离子的控制,并减少D_1处对ClO_2的需求通过改善洗涤过程,从而减少(EOP)洗涤塔中的苏打水残留,并更好地控制进口pH值。同样,发现在漂白纸浆上添加沥青固定剂会使纸浆机白水中较暗的细粉粘结到纤维上,并限制了可达到的纸浆最终亮度。通过使用滑石粉适当分散沥青可以解决此问题。

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