首页> 外文会议>Meeting of the Pulp and Paper Technical Association of Canada >REVISED STEADY-STATE MODEL FOR CHLORINE DIOXIDE BRIGHTENING THAT CONSIDERS EXTRACTION WASHER CARRYOVER EFFECTS
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REVISED STEADY-STATE MODEL FOR CHLORINE DIOXIDE BRIGHTENING THAT CONSIDERS EXTRACTION WASHER CARRYOVER EFFECTS

机译:对二氧化氯增白的修改稳态模型,其考虑提取垫圈携带效应

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In an earlier investigation, a generalized model was developed to simulate the first chlorine dioxide brightening stage (D|). This stoichiometric model accurately predicts pulp brightness values for given bleach charges and vice versa for laboratory softwood pulps. The equation parameters are dependent upon the kappa number and brightness of the extracted pulp. In this study, the above model was refined to include the negative effects of extraction carryover to simulate more realistically a mill's D1 stage. It was found that extracted pulps that contain washer carryover brighten as if the pulp had a kappa number equal to the sum of the extracted kappa and the kappa value of extraction dissolved solids. If this higher kappa (i.e., apparent or wet kappa) is used in place of the extracted kappa with the D1 model, the equations suitably predicted the bleached brightness for a given bleach charge. The modified expressions were used to quantify the amount of carryover and to calculate carryover bleach consumption for a softwood D0(EOP)D1 fiber line. It was determined that the mill's washed pulps had carryover levels of 1.4 kappa units, which was consuming 48% of the total D1 bleach charge. Additional analyses revealed that extraction carryover consumes 2.5 to 4.6 kg ClO2/t pulp per kappa unit of carryover when bleaching a pulp to 78 to 84% ISO. Application: Revised model forecasts pulp brightness for extracted softwood kraft pulps for a variety of chlorine dioxide, extracted kappa and washer carryover levels. Model can be used to analyze bleach plant data to determine extraction washer carryover and bleach consumption caused by this material. Other applications include bleach plant optimizations, process control strategies, and computer simulations.
机译:在早期的研究中,开发了广义模型以模拟第一氯二氧化氯增白阶段(D |)。该化学计量模型精确地预测给定漂白电荷的纸浆亮度值,对实验室软木纸浆反之亦然。等式参数取决于提取的纸浆的κ数和亮度。在这项研究中,上述模型被精制地包括提取携带的负面影响,以模拟研磨机的D1阶段。发现,含有垫圈携带的纸浆,呈纸浆,好像纸浆具有等于提取的κ和萃取的kappa值的Kappa数等于提取的κ溶解的固体。如果使用该较高的Kappa(即,表观或湿κ)用D1模型代替提取的Kappa,则该等式适当地预测给定漂白剂的漂白亮度。改性表达式用于量化携带量,并计算软木D0(EOP)D1纤维线的携带漂白剂消耗。确定轧机的洗涤纸浆具有1.4 kappa单位的携带水平,占总D1漂白剂的48%。额外的分析显示,当将纸浆漂白至78至84%ISO时,萃取携带在每kappa携带单位的情况下消耗2.5至4.6kg Clo2 / T纸浆。应用:修订模型预测纸浆亮度为各种二氧化氯,提取的Kappa和洗衣机携带水平提取。模型可用于分析漂白设备数据以确定由该材料引起的提取垫圈携带和漂白剂消耗。其他应用包括漂白设备优化,过程控制策略和计算机模拟。

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