Apparatus for continuously introducing or removing gases into and/or
from liquids
    1.
    发明授权
    Apparatus for continuously introducing or removing gases into and/or from liquids 失效
    用于连续地将气体引入或从液体中取出和/

    公开(公告)号:US4789469A

    公开(公告)日:1988-12-06

    申请号:US1641

    申请日:1986-12-04

    Abstract: For the purpose of introducing or removing gases into liquids or out of liquids, in particular substrates being subject to a biological conversion, rotating plates (3) are immersed into the liquid phase. The plates (3) are rotatably arranged within a tubular receptacle (1) and arranged in at least one axial section such that they alternately include with the axis (2) of rotation extending in parallel relation to the liquid level an angle of more and less than 90.degree.. Shut-off valves (9) for the gas supply conduit and for the gas discharge conduit are connected to the tubular container (1). The plates (3) are provided with a rough surface and are preferably formed of a porous, in particular foamed, material, wire mesh, wire grating or expanded metal sheet. (FIG. 1)

    Abstract translation: PCT No.PCT / AT86 / 00029 Sec。 一九八六年十二月四日 102(e)日期1986年12月4日PCT提交1986年4月9日PCT公布。 公开号WO86 / 06060 日期为1986年10月23日。为了将气体引入或除去液体或液体,特别是经历生物转化的基底,将旋转板(3)浸入液相中。 板(3)可旋转地布置在管状容器(1)内并且布置在至少一个轴向部分中,使得它们交替地包括与旋转轴线(2)平行延伸的旋转轴线(2),其角度越来越大 90度以上。 用于气体供应管道和气体排出管道的截止阀(9)连接到管状容器(1)。 板(3)设置有粗糙表面,并且优选地由多孔的,特别是发泡的材料,金属丝网,金属丝格栅或膨胀金属板形成。 (图。

    Process for enzymatically saccharifying starch-containing raw-materials
    3.
    发明授权
    Process for enzymatically saccharifying starch-containing raw-materials 失效
    含淀粉原料酶法糖化的工艺

    公开(公告)号:US4749651A

    公开(公告)日:1988-06-07

    申请号:US570284

    申请日:1984-01-12

    CPC classification number: C12P19/14 C12P19/20 C13K1/06 Y10S435/813

    Abstract: In an enzymatic saccharification process, a sugar solution of constant sugar content is obtained by adding to the starch-containing raw materials, prior to the enzymatic saccharification step, part of the sugar solution obtained after the saccharification step and being separated from solid material and having been brought to a higher concentration, so that a higher sugar content, in particular within the range from 15 to 22% by weight and preferably approximately 20% by weight, can constantly be maintained, independent of the concentration and quality of the raw materials.

    Abstract translation: 在酶促糖化方法中,通过在酶促糖化步骤之前向含淀粉的原料中加入部分在糖化步骤后获得的糖溶液并与固体物质分离并且具有 使其具有更高的浓度,因此与原料的浓度和质量无关,可以不断维持更高的糖含量,特别是在15至22重量%,优选约20重量%的范围内。

    Apparatus for continuously separating liquid phases of different density
    4.
    发明授权
    Apparatus for continuously separating liquid phases of different density 失效
    用于连续分离不同密度液相的装置

    公开(公告)号:US4734193A

    公开(公告)日:1988-03-29

    申请号:US907380

    申请日:1986-09-15

    CPC classification number: B01D17/0211 Y10S210/923

    Abstract: The apparatus for continuously separating liquid phases of different density consists of a separating basin (1) within which are arranged partition walls (5) for being lifted and lowered and for being moved one in direction to the other or for being swivelled. Swivelling of the partition walls (5) is effected about an eccentrically arranged axis (7) such that during the swivelling movement the partition walls (5) are simultaneously lifted or lowered. The partition walls (5) can be driven by push rods (8) and thus be swivelled in the contrary sense. When swivelling the partition walls (5) in one direction, the liquid level is lifted in the chamber defined between the partition walls and is lowered in the adjacent chamber, noting that the portion having the lower specific gravity flows over the upper edge, assuming a lower level, of the one partition wall in one direction (11) and that the proportion having the higher specific gravity flows in direction of the arrow (12), i.e. in the opposite direction, below the bottom edge of the outer partition wall (5). The separated phases are collected at the front sides of the separating basin (1). Supply is effected by a supply means (10) approximately centrally of the separating basin (1).

    Abstract translation: 用于连续分离不同密度的液相的装置包括分离池(1),其中分隔壁(1)设置有用于升降的分隔壁(5),并使其沿另一方向移动或者被转动。 分隔壁(5)的旋转围绕偏心布置的轴线(7)进行,使得在旋转运动期间,分隔壁(5)同时被提升或降低。 分隔壁(5)可以由推杆(8)驱动,因此以相反的方式旋转。 当在一个方向上旋转分隔壁(5)时,液面在限定在隔壁之间的室中提升,并且在相邻的室中降低,注意到具有较低比重的部分流过上边缘,假定 在一个方向(11)上的一个分隔壁的较低水平,并且具有较高比重的比例沿着箭头(12)的方向流动,即在相反的方向上在外部分隔壁(5)的底部边缘下方 )。 在分离池(1)的前侧收集分离的相。 供应由分离池(1)的大致中央的供应装置(10)进行。

    Apparatus for separating dust from gases
    5.
    发明授权
    Apparatus for separating dust from gases 失效
    用于分离灰尘与气体的装置

    公开(公告)号:US4756729A

    公开(公告)日:1988-07-12

    申请号:US867557

    申请日:1986-05-28

    CPC classification number: B04C5/103 B01D45/12 B04C5/12 B04C5/14 B04C7/00

    Abstract: In an apparatus for separating dust from gases, the gases are caused to flow in a rotating stream (3) within a substantially tubular and/or conical housing (1). A guiding body (9) extends in axial direction of the housing (1). Gas supply is effected via a supply slot (2) and the discharge opening (10) for pure gas is formed of a gap surrounding the guiding body (9), in particular by a tube (13) surrounding the guiding body (9) with formation of a gap. The dust discharge openings are designed as annular slots (7) located adjacent the inner wall (6) of the housing (1). A dust collecting bunker (5) is connected to the bottom of the housing.

    Abstract translation: 在用于从气体中分离灰尘的装置中,使气体以基本上管状和/或锥形壳体(1)内的旋转流(3)流动。 引导体(9)在壳体(1)的轴向方向上延伸。 气体供应通过供应槽(2)进行,并且用于纯净气体的排放口(10)由围绕引导体(9)的间隙形成,特别是围绕引导体(9)的管(13) 形成差距。 灰尘排出口设计成邻近壳体(1)的内壁(6)的环形槽(7)。 集尘仓(5)连接到外壳的底部。

    Solid jacket centrifuge
    6.
    发明授权
    Solid jacket centrifuge 失效
    固体夹套离心机

    公开(公告)号:US4685899A

    公开(公告)日:1987-08-11

    申请号:US724963

    申请日:1985-04-19

    CPC classification number: B04B11/04 B04B1/02 B04B3/02

    Abstract: The solid jacket centrifuge is a plural chamber centrifuge (1). A housing (2) is, together with the centrifuge, stationarily supported, noting that a carrier (6) for cylindrical mantle surfaces (7 and 8) is provided within the housing (2). The cylindrical mantle surfaces (7 and 8) delimit annular chambers (9 and 10) and are shiftable in the direction of the axis of the shaft (3). There is further provided a screw conveyor (12) for introducing the material to be dewatered. The material to be dewatered enters the first annular chamber (9) via radial channels (15). By shifting the cylindrical mantle surface (7) in the axial direction, the material is discharged in a radial direction into the concentric greater annular chamber (10). When subsequently the mantle surface (8) is moved in the axial direction, discharge is again effected in the radial direction.

    Abstract translation: 固体夹套离心机是多室离心机(1)。 壳体(2)与离心机一起被固定地支撑,注意到在壳体(2)内设置有用于圆柱形套筒表面(7和8)的托架(6)。 圆柱形地幔表面(7和8)限定了环形室(9和10),并且可以在轴(3)的轴线方向上移动。 还设置有用于引入待脱水材料的螺旋输送机(12)。 要脱水的材料通过径向通道(15)进入第一环形室(9)。 通过沿轴向移动圆柱形套筒表面(7),材料沿径向方向排放到同心较大的环形室(10)中。 当随后的地幔表面(8)沿轴向移动时,再次沿径向进行放电。

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