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    • 32. 发明授权
    • Method and apparatus for withdrawing a layer of material from a vessel
    • 从容器中取出材料层的方法和装置
    • US4622141A
    • 1986-11-11
    • US665560
    • 1984-10-29
    • Eli SalemRaymond J. MullerStanley T. Stracey
    • Eli SalemRaymond J. MullerStanley T. Stracey
    • B01J49/00B03B5/30B03B5/62B03B11/00B03B5/64
    • B03B11/00B01J49/0043B03B5/30B03B5/623
    • A method and apparatus is provided for holding first material along with less dense material in substantially separate layers and for effecting removal of at least some of the second material to a location displaced from the layer. The materials are arranged in the two layers with the first material at the bottom of a vessel and with the second material disposed above the first material. An elongate withdrawal conduit projects into the vessel to define (1) an exit port at the wall of the vessel, (2) a confined flow passageway communicating with the exit port within the vessel, and (3) at least one withdrawal aperture with the uppermost portion of any withdrawal aperture being lower than the uppermost portion of the exit port. The upper surface of the first material layer is maintained below the conduit while flow of the second material from the second material layer is effected into and through the conduit via the withdrawal aperture.
    • 提供了一种方法和装置,用于将第一材料与不太致密的材料一起保持在基本上分离的层中,并且用于将至少一些第二材料移除到从该层移位的位置。 这些材料被布置在两层中,第一种材料位于容器底部,第二种材料设置在第一种材料之上。 细长的取出导管伸入容器中以限定(1)在容器壁处的出口,(2)与容器内的出口连通的密闭流动通道,和(3)至少一个抽出孔,其中 任何取出孔的最上部比出口的最上部低。 第一材料层的上表面保持在管道下方,同时来自第二材料层的第二材料的流动通过抽出孔进入和穿过导管。
    • 33. 发明授权
    • Hydraulic concentrator
    • 液压集中器
    • US4620689A
    • 1986-11-04
    • US730758
    • 1985-05-03
    • Edward J. Pierce
    • Edward J. Pierce
    • B03B5/62B03B5/68B03B7/00B03B11/00F16L55/14
    • B03B7/00B03B11/00B03B5/62B03B5/626B03B5/68
    • The invention includes a concentrator that pressurizes and provides an enriched liquid suspension to a separator. In the concentrator, the incoming liquid suspension is driven by a diaphragm pump into a funnel-shaped accumulator that is closed at its top. Some of the heavier particles go directly to the bottom of the accumulator, but the lighter particles and the remainder of the suspension are forced to flow through tubes that extend from the top of the accumulator upward on a helical path. Further particulate matter settles out in the helical passages and migrates to the bottom of the accumulator. From the accumulator, the concentrated suspension is fed under pressure to a separator that includes an inclined chamber that is completely filled with liquid. A stream of wash water is directed from the lower rear end of the separator towards the upper front end of the separator. An island in the separator includes a rearwardly opening passage through which the enriched suspension from the concentrator enters the separator. The floor and ceiling of the separator chamber define between them an undulating passage from the back end to the front end of separator. The separated material is discharged from the separator through a unique pinch valve, while the wash water and finer particles are forced from the front end of the separator chamber through an upwardly directed helical path which provides further separation.
    • 本发明包括一个浓缩器,其将分离器的富集的液体悬浮液加压并提供。 在浓缩器中,进入的液体悬浮液由隔膜泵驱动到在其顶部封闭的漏斗状储液器中。 一些较重的颗粒直接进入蓄能器的底部,但是较轻的颗粒和悬浮液的其余部分被迫流过从累积器的顶部在螺旋路径上向上延伸的管。 另外的颗粒物质在螺旋通道中沉降并迁移到蓄能器的底部。 从蓄液器中,将浓缩的悬浮液在压力下进料到包括完全充满液体的倾斜室的分离器中。 洗涤水流从分离器的下后端朝向分离器的上前端引导。 分离器中的岛包括向后开口的通道,浓缩器的富集悬浮液通过该通道进入分离器。 分离器室的地板和天花板在它们之间限定了从分离器的后端到前端的起伏通道。 分离的材料通过独特的夹管阀从分离器排出,同时洗涤水和更细的颗粒从分离器室的前端通过向上的螺旋路径被强制提供进一步的分离。
    • 34. 发明授权
    • Hydraulic concentrator
    • 液压集中器
    • US4529508A
    • 1985-07-16
    • US573056
    • 1984-01-23
    • Edward J. Pierce
    • Edward J. Pierce
    • B03B5/62B03B5/68B03B7/00B03B11/00B03B5/66
    • B03B7/00B03B11/00B03B5/62B03B5/626B03B5/68
    • The invention includes a concentrator that pressurizes and provides an enriched liquid suspension to a separator. In the concentrator, the incoming liquid suspension is driven by a diaphragm pump into a funnel-shaped accumulator that is closed at its top. Some of the heavier particles go directly to the bottom of the accumulator, but the lighter particles and the remainder of the suspension are forced to flow through tubes that extend from the top of the accumulator upward on a helical path. Further particulate matter settles out in the helical passages and migrates to the bottom of the accumulator. From the accumulator, the concentrated suspension is fed under pressure to a separator that includes an inclined chamber that is completely filled with liquid. A stream of wash water is directed from the lower rear end of the separator towards the upper front end of the separator. An island in the separator includes a rearwardly opening passage through which the enriched suspension from the concentrator enters the separator. The floor and ceiling of the separator chamber define between them an undulating passage from the back end to the front end of the separator. The separated materials discharged from the separator through a unique pinch valve, while the wash water and finer particles are forced from the front end of the separator chamber through an upwardly directed helical path which provides further separation.
    • 本发明包括一个浓缩器,其将分离器的富集的液体悬浮液加压并提供。 在浓缩器中,进入的液体悬浮液由隔膜泵驱动到在其顶部封闭的漏斗状储液器中。 一些较重的颗粒直接进入蓄能器的底部,但是较轻的颗粒和悬浮液的其余部分被迫流过从累积器的顶部在螺旋路径上向上延伸的管。 另外的颗粒物质在螺旋通道中沉降并迁移到蓄能器的底部。 从蓄液器中,将浓缩的悬浮液在压力下进料到包括完全充满液体的倾斜室的分离器中。 洗涤水流从分离器的下后端朝向分离器的上前端引导。 分离器中的岛包括向后开口的通道,浓缩器的富集悬浮液通过该通道进入分离器。 分离器室的地板和天花板在它们之间限定从分离器的后端到前端的起伏通道。 分离的材料通过独特的夹管阀从分离器排出,而洗涤水和更细的颗粒从分离器室的前端通过向上指向的螺旋路径被迫使其进一步分离。
    • 35. 发明授权
    • Float-and-sink separator
    • 浮动和水槽分离器
    • US4379048A
    • 1983-04-05
    • US314082
    • 1981-10-13
    • Johann J. Jansen
    • Johann J. Jansen
    • B03B5/28B03B11/00B03B5/36
    • B03B11/00
    • Washing tank for separating particles differing the specific gravity by means of a liquid separatory medium using the float-and-sink method. The washing tank is provided with at least one collecting tray for removing the settled particles, which collecting tray can be reciprocated along the bottom of the washing tank and in the first extreme position is about centrally on the bottom of the washing tank, where it can collect settling particles, and in the second extreme positions rests on the edge of the washing tank, so tilted that settled particles contained in it can slide into a discharge device positioned next to the washing tank. Preferably, the washing tank is provided with two alternating collecting trays hingingly attached to arms fixed on a horizontal shaft swinging to and fro between two extreme positions.
    • PCT No.PCT / NL81 / 00002 Sec。 371日期1981年10月13日 102(e)1981年10月13日,PCT提交1981年2月13日PCT公布。 公开号WO81 / 02259 日期1981年8月20日。使用浮法和沉降法通过液体分离介质分离不同比重的颗粒的洗涤槽。 洗涤槽设置有至少一个用于去除沉降的颗粒的收集盘,该收集盘可以沿着洗涤槽的底部往复运动,并且在第一极限位置处于洗涤槽的底部大约中央 收集沉降颗粒,并且在第二极限位置搁置在洗涤槽的边缘上,因此倾斜,其中包含的沉淀颗粒可以滑入位于洗涤槽旁边的排放装置中。 优选地,洗涤槽设置有两个交替的收集托盘,其铰接地附接到固定在两个极端位置之间来回摆动的水平轴上的臂上。
    • 36. 发明授权
    • Separable means for excluding oversized slender objects
    • 可分离的手段,用于排除超大的细长物体
    • US4367601A
    • 1983-01-11
    • US232862
    • 1981-02-09
    • John P. LatimerJohn H. Hall
    • John P. LatimerJohn H. Hall
    • B03B11/00E02F3/92E02F3/94
    • E02F3/94B03B11/00E02F3/92
    • For screening oversized objects and especially long slender particles wherein the long dimension of the particle is aligned in the direction of flow through a fluid-flow conduit, there is provided a screen comprising a pair of opposing corrugated surfaces, the folds or corrugations on the opposing surfaces being substantially parallel, and separated by a distance, and having a wave length, determined by the size particle to be screened. Preferably, the corrugated surfaces are formed as two sets of a plurality of corrugated plates inserted within and extending along the direction of fluid-flow in a conduit, the sets being relatively movable between a position where the two sets are interleaved, and a position where the two are separated.
    • 为了筛选尺寸过大的物体,特别是长度细长的颗粒,其中颗粒的长尺寸沿着流过流体导管的流动方向排列,提供了一个包括一对相对的波纹表面的筛网,相对的折叠或波纹 表面基本上平行,并且分开一段距离,并且具有由待筛选的尺寸颗粒确定的波长。 优选地,波纹状表面形成为插入管道中的流体流动方向并沿其延伸的两组多个波纹板,所述多个波纹板在两组交错的位置之间可相对移动, 两者分开。