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Cleaning of used paper and cellulose suspensions uses an eddy chamber for the suspension where injected water flows at a high relative speed to separate particles and gels and break up fiber clumps
Cleaning of used paper and cellulose suspensions uses an eddy chamber for the suspension where injected water flows at a high relative speed to separate particles and gels and break up fiber clumps
To detach particles and gels from suspended paper materials, and break up paper fiber clumps, the suspension (S) is subjected to a water (W) flow from a number of flow channels (1,1') with a high relative speed of at least 30 m/s, to give the particle separation and break-up action. The relative flow speed (V1) is at least 60 m/s. On entry into the system the suspension (S) is moved in a flow, with a speed component aligned against the water (W) emerging from the channels (1,1'). A flow channel (1') has a narrowed section, along part of its length, to accelerate the water (W) flow, in the form of a tapering conical jet. The smallest clear width of the water flow channel (1) is max. 10 mm. The suspension (S) is passed through an eddy chamber (2), where at least one water flow channel (1) opens into it. The flow vol. of the water (W) is at least 20% of the fiber suspension (S) flow vol. The water flow vol. through a flow channel (1) is max. 2 l/s. The suspension (S) has a solid content of = 6%, and is mostly of used paper.
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机译:为了从悬浮的纸张材料中分离出颗粒和凝胶,并使纸张纤维团破裂,悬浮液(S)受到来自多个流道(1,1')的水(W)的高速流动,相对速度为至少30 m / s,以实现颗粒分离和破碎作用。相对流速(V1)至少为60 m / s。进入系统后,悬浮液(S)以流动方式运动,速度分量与从通道(1,1')流出的水(W)对齐。流动通道(1')沿其长度的一部分具有变窄的截面,以逐渐变细的锥形射流的形式加速水(W)的流动。水流通道(1)的最小净宽度最大。 10毫米悬浮液(S)通过涡流室(2),其中至少一个水流通道(1)进入涡流室。流量水(W)的至少10%是纤维悬浮液(S)的流量的20%。水流量通过流道(1)的流量最大。 2升/秒悬浮液(S)的固体含量<= 6%,并且大部分为废纸。
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