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Process for pulping and cleaning of fibrous material containing impurities in particular waste paper

机译:将特别是废纸中含有杂质的纤维材料制浆和清洁的方法

摘要

For the repulping and cleaning of a paper fiber suspension (P1), and especially used paper for recycling, the overflow fraction (5) from the coarse matter screening (2) is taken off in a time duration of at least 80% of the operating time to give a cleaned suspension flow (4). The volume flow of the overflow fraction is set at a minimum of 15% of the inflow into the coarse screening stage and a maximum of 50%. The overflow fraction is passed to a further screening station (3) where waste matter is spun out intermittently as an overflow fraction (5') to give an additional cleaned suspension flow (4'). For repulping and cleaning a used paper fiber suspension, the overflow from the coarse screening stage is taken off until no impurities are spun out of the further screening stage. The cleaned suspension flow is taken off continuously from the coarse screening stage. The spinning out of impurities from the further screening is effected where the overflow into the stage is stopped and, in this time, a flushing flow (W) is pumped into the screening stage to carry out waste matter through a further overflow containing impurities. On spinning, all the waste matter is taken out of the further screening stage while the outflow of cleaned suspension is halted. The two flows of cleaned suspension are brought together. The overflow from the second screening stage is passed to a sorting drum (8), where a reject fraction (11) is formed as an overflow, and the cleaned flow from the drum is returned to the repulping assembly. The overflow from the second screening stage is thickened in a press. The overflow volume from the coarse screening stage is set at 20-30% of the inflow volume into the screening stage. The volume of fibers in the overflow from the second screening stage is set at 20-30% of the fiber content of the inflow to the second screening. The coarse screening uses a sieve with openings in a maximum width of 4 mm. It is a flat sieve, cleared by a moving sieve cleaner. The soiled fiber suspension can be fed centrally into the coarse screening stage, where heavy waste is separated by a heavy particle centrifuge. Between the pulper and the coarse screening stage either no impurities are removed or only coarse particles are extracted which would be rejected by a sieve with openings of maximum 30 mm diameter, separated by a rotating sieve drum with openings of a maximum 30 mm diameter. The repulping stage has a drum, with a screening unit as an axial extension of it. The pulping drum is operated to generate a constant flow of pulp (P), to be diluted by water (W') into a soiled pulp flow. The pulper is a high consistency pulper (1), operated intermittently, with its outflow diluted with water into the required consistency for the coarse screening stage. The inner volume of the coarse screening unit, at the feed side, is at least 15% of the volume of the outflow which would fill the machine in 1 min. The inner volume of the feed side of the second screening stage is at least 30% of the volume of the outflow which would fill this machine in 1 min.
机译:为了对纸纤维悬浮液(P1)进行重新浆化和清洁,尤其是用于回收的废纸,应在至少80%的运行时间内从粗筛(2)中排出溢流馏分(5)。时间给出清洁的悬浮液(4)。溢流部分的体积流量设置为流入粗筛阶段的最小流量的15%,最大50%。溢流部分进入另一个筛选站(3),在这里,废物作为溢流部分(5')间歇地甩出,以提供额外的清洁悬浮液(4')。为了再制浆和清洁用过的纸纤维悬浮液,将粗筛分阶段的溢流排出,直到没有杂质从进一步的筛分阶段流出。从粗筛阶段开始连续排出清洗后的悬浮液。在进一步停止筛分的过程中将杂质从筛分中分离出来,此时停止向该阶段的溢流,此时,将冲洗流(W)泵入筛分阶段,以通过含杂质的另一次溢流进行废物处理。纺纱时,所有废物均从进一步的筛选阶段中取出,同时停止了清洁后的悬浮液的流出。清洗后的悬浮液的两个流汇合在一起。来自第二筛分阶段的溢流被传递到分选鼓(8),在分选鼓(8)中形成废品部分(11)作为溢流,并且来自鼓的清洁后的流返回到重新制浆组件。来自第二筛分阶段的溢流在压机中被浓缩。粗筛阶段的溢流体积设定为筛阶段流入量的20-30%。将来自第二筛分阶段的溢流中的纤维体积设定为进入第二筛分的入流纤维含量的20-30%。粗筛使用筛网,筛网的最大宽度为4 mm。它是一个平筛,由移动的筛清洁器清除。可以将污染的纤维悬浮液集中送入粗筛阶段,在粗筛阶段中,将重废料通过重颗粒离心机分离。在碎浆机和粗筛阶段之间,不会除去任何杂质,或仅提取出粗颗粒,这些粗颗粒将被最大孔径为30 mm的筛子筛分,并被最大孔径为30 mm的旋转筛鼓隔开。粉碎阶段具有转鼓,转鼓的轴向延伸部分带有筛分单元。操作制浆滚筒以产生恒定的纸浆流(P),然后将其用水(W')稀释成脏的纸浆流。碎浆机是一种高浓度碎浆机(1),间歇运行,其出水用水稀释成粗筛阶段所需的稠度。粗筛分装置在进料侧的内部容积至少为流出液的15%,该流出量将在1分钟内充满机器。第二个筛分阶段进料侧的内部体积至少为流出液的30%,而流出液将在1分钟内充满该机器。

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