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    • 2. 发明授权
    • Process and device to drain a fibrous pulp suspension
    • 排出纤维纸浆悬浮液的方法和装置
    • US6042735A
    • 2000-03-28
    • US921023
    • 1997-08-29
    • Axel GommelHerbert HolikJosef Schneid
    • Axel GommelHerbert HolikJosef Schneid
    • D21F1/78D21F1/80B01D37/00B01D33/044B01D33/048
    • D21F1/78D21F1/80
    • Process and device for draining a fibrous pulp suspension. The process may include positioning two surfaces to converge in a downstream direction, feeding the fibrous pulp suspension between the two converging surfaces, driving at least one of the two converging surfaces to move the suspension with a relative translational velocity, and draining the fibrous pulp suspension through each of the two surfaces. The device may include two arcuate surfaces positioned to form converging surfaces. One of the two arcuate surfaces may include a drivable, pivotable, and rotatable cylinder having an outer sleeve with openings, the other of the two arcuate surfaces may include a screen positioned to be guided around at least a portion of the outer sleeve. The screen and the openings may form drains for draining the fluid pulp suspension.
    • 用于排出纤维纸浆悬浮液的方法和装置。 该方法可以包括将两个表面定位成在下游方向上会聚,将纤维纸浆悬浮液馈送在两个会聚表面之间,驱动两个会聚表面中的至少一个以相对平移速度移动悬浮液,并排出纤维纸浆悬浮液 通过两个表面中的每一个。 该装置可以包括两个定位成形成会聚表面的弓形表面。 两个弧形表面中的一个可以包括可驱动的,可枢转的和可旋转的圆筒,其具有带有开口的外套筒,两个弧形表面中的另一个可以包括定位成围绕外套筒的至少一部分被引导的筛网。 筛网和开口可以形成用于排出流体纸浆悬浮液的排水沟。
    • 8. 发明授权
    • Method for fabricating a flat or centripetal wire
    • 制造平面或向心线的方法
    • US5768783A
    • 1998-06-23
    • US789196
    • 1997-01-24
    • Werner Lange
    • Werner Lange
    • D21D5/00B01D29/01B07B1/12B07B1/46D21D5/02D21D5/04D21D5/16B21D39/00
    • B07B1/4618B01D29/01B01D29/012B07B1/12B07B1/4681D21D5/16B01D2201/184Y10T29/49604Y10T29/4962Y10T29/49924Y10T29/49925
    • Method of making a flat wire of the type comprising a plurality of bars in substantially axially parallel arrangement relative to one another and including wire slots contained inbetween. Said method comprises providing a plurality of bars and providing at least two bar support members. Each bar support member includes laterally open recesses provided along a longitudinal edge of the bar support member. Each bar support member is capable of being flexed from an initial state to a final state. At the initial state, the longitudinal edge has an initial radius of curvature such that the laterally open recesses are open sufficiently to receive the bars and wherein at the final state, the longitudinal edge has a final radius of curvature larger than the initial radius of curvature such that the laterally open recesses are sufficiently closed to exert a clamping force upon the bars retained in said recesses. The bars are inserted into the laterally open recesses of the bar support members while the bar support members are in the initial state in order to provide a wire shell. The bar support members are bent from the initial state to the final state such that the laterally open recesses exert a clamping force upon the bars.
    • 制造包括多个条的扁平线的方法,所述多个条基本上相对于彼此基本上轴向平行布置,并且包括其间包含的线槽。 所述方法包括提供多个杆并提供至少两个杆支撑构件。 每个杆支撑构件包括沿着杆支撑构件的纵向边缘设置的横向开放的凹部。 每个杆支撑构件能够从初始状态弯曲到最终状态。 在初始状态下,纵向边缘具有初始曲率半径,使得横向开放的凹部足够开放以接收杆,并且其中在最终状态下,纵向边缘具有比初始曲率半径大的最终曲率半径 使得横向敞开的凹陷足够闭合,以对保持在所述凹部中的条施加夹紧力。 杆被插入杆支撑构件的横向开口的凹部中,同时杆支撑构件处于初始状态以便提供线壳。 杆支撑构件从初始状态弯曲到最终状态,使得横向开口的凹部在杆上施加夹紧力。
    • 10. 发明授权
    • Flotation process and mixing device
    • 浮选工艺及混合装置
    • US6129212A
    • 2000-10-10
    • US834457
    • 1997-04-15
    • Jens Muller
    • Jens Muller
    • B03D1/14B03D1/24D21F1/70
    • D21F1/70B03D1/028B03D1/1493B03D1/247
    • The flotation process for separating particulate impurities from fibrous suspensions in a flotation tank. Upon or after entry into the flotation tank, the fibrous suspension added to the flotation tank may be mixed with a portion of the suspension already in the flotation tank. The portion of the suspension already in the flotation tank may be drawn into the added suspension. After mixing, the mixed suspensions enter a mixing element. The mixed suspension is expelled into the flotation tank and a circular flow pattern is generated within the flotation tank as a result. A flow speed may be limited at a top end so that an optimal mixing with the gas bubbles required for flotation may occur with a desired energy savings.
    • 用于从浮选槽中的纤维悬浮液中分离颗粒杂质的浮选工艺。 在进入浮选槽中或之后,添加到浮选槽中的纤维悬浮液可以与已经在浮选槽中的悬浮液的一部分混合。 已经在浮选槽中的悬浮液的部分可以被吸入添加的悬浮液中。 混合后,混合悬浮液进入混合元件。 混合悬浮液被排入浮选槽中,结果在浮选槽内产生循环流动模式。 流速可能在顶端受到限制,从而可以以所需的能量节省与浮选所需的气泡的最佳混合。