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    • 81. 发明公开
    • Noise level reduction of sparger assemblies
    • GeräuschpegelreduzierungfürSprengeranordnungen
    • EP2338588A1
    • 2011-06-29
    • EP11154482.1
    • 2004-07-20
    • Fisher Controls International LLC
    • Catron, Frederick, WayneDePenning, Charles, LawrenceFagerlund, Allen, Carl
    • B01F5/04F01K9/04F01D25/30
    • B01F5/0465B01F5/0453F01D25/30F01K9/04
    • The present invention discloses a system for reducing steam pressure comprising a boiler adapted to generate steam; a condenser; a duct in fluid communication with the boiler and the condenser; and a sparger assembly at least partially disposed within the duct, the sparger assembly comprising a plurality of spargers, each of the plurality of spargers having a centerline axis, an outer diameter, and a plurality of radially-disposed fluid passageways, wherein steam from the boiler is radially emitted from the plurality of fluid passageways of each of the plurality of spargers into the duct, and wherein the distance between the centerline axes of adjacent spargers and the outer diameter of adjacent spargers forms a ratio, and the value of the ratio is between 2 and 5.
    • 本发明公开了一种用于降低蒸汽压力的系统,其包括适于产生蒸汽的锅炉; 冷凝器 与锅炉和冷凝器流体连通的管道; 以及至少部分地设置在所述管道内的分布器组件,所述分布器组件包括多个喷射器,所述多个喷射器中的每一个具有中心线轴线,外径和多个径向设置的流体通道,其中来自 锅炉从多个喷射器中的每一个的多个流体通道径向发射到管道中,并且其中相邻喷射器的中心线轴线之间的距离和相邻喷雾器的外径形成比例,并且该比值的值为 在2到5之间。
    • 87. 发明公开
    • Fluid mixing apparatus and fluid mixing method
    • 流体动力学
    • EP1839733A3
    • 2009-07-01
    • EP07006243.5
    • 2007-03-27
    • FUJIFILM Corporation
    • Fujiwara, Takayuki c/o Fujifilm CorporationOkutsu, Kazuo c/o Fujifilm Corporation
    • B01F13/00B01F5/04B01J19/00
    • B01F13/0067B01F5/0453B01F5/046B01J19/0093B01J2219/00783B01J2219/00819B01J2219/00862B01J2219/00889B01J2219/00891B33Y80/00
    • There is provided a fluid mixing apparatus (10) and a fluid mixing method that can increase uniform distribution properties of fluids in numbering-up and air bubble removing properties in channels to allow uniform and stable mixing or reaction to be performed. The fluid mixing apparatus (10) has a numbering-up mechanism that distributes plural kinds of fluids L1 and L2 and concurrently performs multiple mixing or reactions, including: a rectifying section (28) having a plurality of annular channels (50) and (60) that rectify the plural kinds of fluids L1 and L2 into respective concentric annular flows; a distribution section (30) having a plurality of distribution channels (62)... and (64) ... that distribute the plural kinds of fluids L1 and L2 rectified by the rectifying section (28) into a plurality of flows; a converging section (31) having a plurality of converging channels (92) ... and (94) ... that converge different kinds of fluids among the plural kinds of fluids L1 and L2 distributed by the distribution section (30); and a mixing/reaction section (32) having a plurality of mixing/reaction channels (66) ... that cause mixing or reaction of the plural kinds of fluids L1 and L2 converged by the converging section (31), wherein pressure loss increasing devices are provided in the distribution channels (62) ... and (64) ....
    • 提供一种流体混合装置(10)和流体混合方法,其可以增加通道中的数字和气泡去除性能中流体的均匀分布特性,以允许均匀且稳定的混合或反应进行。 流体混合装置(10)具有分配多种流体L1和L2并同时进行多次混合或反应的编号机构,包括:整流部(28),具有多个环形通道(50)和(60 ),将多种流体L1和L2整流到各个同心的环状流中; 具有多个分配通道(62)...和(64)的分配部分(30),其将由整流部分(28)整流的多种流体L1和L2分配成多个流; 具有会聚不同种类的流体的多个会聚通道(92)的收敛部分(31),该分配通道分配在由分配部分(30)分配的多种流体L1和L2中的各种流体; 以及具有多个混合/反应通道(66)的混合/反应部分(32),其引起由会聚部分(31)收敛的多种流体L1和L2的混合或反应,其中压力损失增加 设备设置在分配通道(62)...和(64)中....
    • 88. 发明公开
    • VERFAHREN UND VORRICHTUNG ZUM VERMISCHEN EINES GASFÖRMIGEN FLUIDS MIT EINEM GROSSEN GASMENGENSTROM, INSBESONDERE ZUM EINBRINGEN EINES REDUKTIONSMITTELS IN EIN STICKOXIDE ENTHALTENDES RAUCHGAS
    • VERFAHREN UND VORRICHTUNG ZUM VERMISCHEN EINESGASFÖRMIGENFLUIDS MIT EINEM GROSSEN GASMENGENSTROM,INSBESONDERE ZUM EINBRINGEN EINES REDUKTIONSMITTELS IN EIN STICKOXIDE ENTHALTENDES RAUCHGAS
    • EP1981622A1
    • 2008-10-22
    • EP07722772.6
    • 2007-01-26
    • FISIA Babcock Environment GmbH
    • BECKMANN, GerdENGELKING, WolframPRIESMEIER, Ulrich
    • B01F3/02B01F3/04B01F5/04B01F5/06B01F15/00B01D53/34B01D53/76F23J15/00
    • B01D53/8631B01D53/90B01D2251/20B01F3/02B01F3/04021B01F5/0451B01F5/0453B01F5/0458B01F5/0618B01F2005/0017F23J15/003
    • A process is disclosed for mixing a fluid stream (F) with a large flow-rate gas stream (2), in particular for introducing a reducing agent into flue gas containing nitrogen oxides, in which process the large flow-rate gas stream impinges against the inflow side of at least one disk-like mixer element (1; 8) arranged at an angle against the direction of flow, and across which eddy currents (3) are formed, and the fluid stream is added to the large flow-rate gas stream downstream from the mixer element. In order to mix the fluid stream more completely with the large flow-rate gas stream, the fluid stream is added in the form of a swirling flow (7; 10). For that purpose, the swirling fluid flow is preferably led on the outflow side (8b) (lee side) of the mixer element (8) substantially perpendicularly to the mixer element (8) and substantially towards the centre (M) of the mixer element, and the fluid enters the eddy current from the centre of the mixer element, past its outflow side. However, it is also possible for the swirling fluid flow to be led on the inflow side (1a) (windward side) substantially perpendicularly to the mixer element (1) and to exit through an opening (8) located substantially in the centre (M) of the mixer element, on the outflow side (1b) (lee side) of the mixer element, and for the fluid to enter the eddy current from the centre of the mixer element, past the outflow side. The invention is also directed to a corresponding device.
    • 公开了一种用于将流体流(F)与大流量气流(2)混合,特别是用于将还原剂引入含氮氧化物的烟道气中的方法,在该方法中,大流率气流撞击 至少一个盘形混合器元件(1; 8)的流入侧以与流动方向成一定角度布置,并且涡流(3)形成于其上,并且流体流被添加到大流量 从混合器元件下游的气流。 为了使流体流更完全地与大流量气流混合,流体流以旋流(7; 10)的形式加入。 为此,旋流流体优选在混合器元件(8)的流出侧(8b)(背风侧)基本上垂直于混合器元件(8)且基本朝向混合器元件(8)的中心(M) ,并且流体从混合器元件的中心经过其流出侧进入涡流。 然而,旋流流体也可以基本上垂直于混合器元件(1)在流入侧(1a)(迎风侧)被引导并且通过基本位于中心(M)的开口(8) )在混合器元件的流出侧(1b)(背风侧),并且流体从混合器元件的中心进入涡流,流过流出侧。 本发明还涉及相应的装置。