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Improvements relating to the separation of gases and other foreign matter from liquids, particularly pulp suspensions

机译:与从液体(尤其是纸浆悬浮液)中分离气体和其他异物有关的改进

摘要

768,537. Centrifugal separators. FREEMAN H., and BOADWAY, J. D. April 27, 1955 [April 27, 1954], No. 12193/55. Addition to 740,588. Class 23 In a method of separating gases and other impurities from a liquid comprising injecting the liquid into a chamber 13 to form a hollow vortex 15, reversing part of the vortex 15 to form a second vortex 20, and reversing part of the vortex 20 to form a third vortex 35 enclosing a gas core 14, the impurities are discharged with the remaining part of the vortex 15, the purified liquid in the remaining part of the vortex 20, and the gas is withdrawn at a rate to maintain a sub-atmospheric pressure in the core. Paper pulp, tangentially injected into the chamber 13 by a nozzle 10, is guided within the chamber by a spiral guide 12 to form the vortex 15. On reaching the bottom section 16 part of the vortex 15 is reversed to form the vortex 20 and the remainder of the vortex 15 carries dirt to the outlet 18. The vortex 20 passes upwardly through the vortex finder 21 to meet a conical projection 27 which reverses a part of the vortex to form the vortex 35 whilst the purified pulp forming the remainder of the vortex 20 passes through an annular gap 29 to a chamber 30 from whence it is discharged by a tangential outlet 32. The vortex 35, which contains gas bubbles, is discharged with the dirty pulp through the outlet 18. As shown, the outlet is connected to a pipe 36 shaped to give an eduction effect which permits discharge to atmosphere, but the outlet may be connected to a vacuum pump particularly if it is desired to remove dissolved gases. In a modification (Fig. 9, not shown) the outlet 18 discharges axially into the upper part of a chamber similar to the chamber 13 and to which water is supplied through the tangential inlet so that the eduction effect on the outlet is increased and the dirty pulp is diluted. In the modification, shown in Fig. 7, the outer part of the vortex 20SP1/SP, constituting the purified pulp, is discharged through perforations in a cylindrical extension 40 of the vortex finder 21SP1/SP to a chamber 42 having an outlet 43. In the separating plant shown in Fig. 8 three separators 13 discharge dirty pulp into a vacuum chamber 46, the dirty pulp from the chamber 46 being separated, after dilution in a further separator 52 and the purified pulp from the separator 52 being returned to the separators 13. Dimensions of the section 16 are given in the Specification.
机译:768,537。离心分离机。 FREEMAN H.和BOADWAY,J. D. 1955年4月27日[1954年4月27日],编号12193/55。除了740,588。 23类:从液体中分离气体和其他杂质的方法,该方法包括将液体注入腔室13中以形成空心涡流15,使涡流15的一部分反向以形成第二涡流20,并且使涡流20的一部分反向以形成第二涡流20。形成一个包围着气芯14的第三涡流35,杂质与涡流15的其余部分一起排出,净化液体在涡流20的其余部分中排出,并以保持低于大气压的速率抽出气体核心压力。由喷嘴10切向注入腔室13中的纸浆在螺旋腔室中由螺旋导向器12引导以形成涡旋15。在到达底部16时,涡旋15的一部分被反转以形成涡旋20,并且旋涡15的其余部分将污物运送到出口18。旋涡20向上穿过旋涡探测器21,以遇到圆锥形突出部27,该圆锥形突出部使旋涡的一部分反转以形成旋涡35,而纯化的纸浆形成旋涡的其余部分。图20中的空气通过环形间隙29到达腔室30,从那里通过切向出口32排出。包含气泡的涡旋35与脏纸浆一起通过出口18排出。如图所示,出口连接到管道36的形状做成能产生允许排放到大气中的排放效果,但是出口可以连接到真空泵上,特别是在需要除去溶解气体的情况下。在一种改型(图9,未示出)中,出口18轴向排放到类似于腔室13的腔室的上部,并且通过切向入口向其供应水,从而增加了对出口的排放效果,并且脏浆被稀释。在该变形例中,如图7所示,构成净化纸浆的涡旋20 1 的外部通过在涡旋发现器21 1 <到具有出口43的腔室42中。在图8所示的分离设备中,三个分离器13将脏纸浆排放到真空腔室46中,在另一个分离器52中稀释之后,将来自腔室46的脏纸浆分离。分离器52的纯化纸浆返回分离器13。在说明书中给出了部分16的尺寸。

著录项

  • 公开/公告号GB768537A

    专利类型

  • 公开/公告日1957-02-20

    原文格式PDF

  • 申请/专利权人 HORACE FREEMAN;JOHN DOUGLAS BOADWAY;

    申请/专利号GB19550012193

  • 发明设计人

    申请日1955-04-27

  • 分类号B01D19/00;B01D21/00;B04C3/00;B04C5/081;B04C5/107;B04C5/12;B04C5/14;B04C5/15;B04C5/18;B04C5/185;D21D5/18;D21D5/24;D21D5/26;

  • 国家 GB

  • 入库时间 2022-08-23 22:12:25

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