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Wood-pulping equipment for paper- or card manufacture, employs compression refiner to complete fiber hydration and separation without damage

机译:用于造纸或卡片生产的木材制浆设备,使用压缩磨浆机完成纤维的水合和分离,而不会造成损坏

摘要

Soaked wood particles (S) with excess water, are processed to a fibrous pulp (S2) using a compression refiner (1). The wood particles are processed in a crushing zone between surfaces (4, 5) with rolling contact. The surfaces (4, 5) are external to crushing rollers (6) and internal (or external) to a rotating drum (3). Speeds of the contact surfaces differ by 10%. The consistency produced by the compression refiner is preferably 10%-20%. A specific energy consumption in the compression refiner of 400-600 kWh/t, produces pulp for card manufacture, with a specific volume of 2 cm3/g. Specific energy consumption of 800-1200 kWh/t, is used to manufacture graphic paper. The compression zone temperature is 30-50[deg]C. The temperature in the compression refiner is 70-130[deg]C. The soaked wood particles have a maximum preferred thickness of 1-3 mm. They are flat wood chips no more than 5 mm thick. Material used as wood particles result from driving a wood grinder at reduced power. The particles are soaked in water and chemicals (CH), swelling the cellulose and softening or embrittling the lignin. The pulp (S2) passes through a pressure sorter (10), which rejects (R) insufficiently-pulped components. The pulp (S2) is divided into fractions in a hydrocyclone (11), with similar oversize rejection. Reject material (R) is recycled to the compression refiner. Separated components may be further processed in a further compression refiner. They may be ground conventionally, to a consistency of 2% to 6%.
机译:使用压缩磨浆机(1)将浸有过量水的木屑(S)加工成纤维浆(S2)。木材颗粒在表面(4、5)之间的破碎区域中滚动接触进行处理。表面(4、5)在破碎辊(6)的外部,并且在旋转鼓(3)的内部(或外部)。接触面的速度相差10%。压缩磨浆机产生的稠度优选为10%-20%。压缩磨浆机中的单位能耗为400-600 kWh / t,生产出的纸浆生产纸浆的单位体积为2 cm3> / g。比能耗为800-1200 kWh / t,用于生产图形纸。压缩区温度为30-50℃。压缩磨浆机中的温度为70-130℃。浸泡的木颗粒的最大优选厚度为1-3mm。它们是厚度不超过5毫米的扁平木片。用作木屑的材料是由降低功率驱动木磨机产生的。将颗粒浸泡在水和化学药品(CH)中,使纤维素溶胀并使木质素软化或脆化。纸浆(S2)通过压力分选器(10),该分选器剔除(R)原料不足的成分。纸浆(S2)在水力旋流器(11)中分成多个部分,并具有类似的超大排料率。废料(R)循环至压缩磨浆机。分离的组分可以在另一个压缩磨浆机中进一步处理。可以按照常规方式将它们研磨到2%至6%的稠度。

著录项

  • 公开/公告号DE102007003964A1

    专利类型

  • 公开/公告日2008-01-24

    原文格式PDF

  • 申请/专利权人 VOITH PATENT GMBH;

    申请/专利号DE20071003964

  • 发明设计人 LUEDTKE OLIVER;RAPP ALEXANDER;

    申请日2007-01-26

  • 分类号D21B1/14;D21C1/00;

  • 国家 DE

  • 入库时间 2022-08-21 19:49:25

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