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公开(公告)号:WO2015148279A1
公开(公告)日:2015-10-01
申请号:PCT/US2015/021622
申请日:2015-03-20
申请人: CORNING INCORPORATED
CPC分类号: B01J19/123 , B01J19/127 , B01J19/249 , B01J2219/0871 , B01J2219/0877 , B01J2219/0888 , B01J2219/1206 , B01J2219/1281 , B01J2219/1296 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2483 , B01J2219/2496
摘要: A modular photochemical reactor system comprises a plurality of fluidic modules (20) each having i) a central planar process fluid layer (30) and ii) two outer planar thermal control fluid layers (40) for containing flowing thermal control fluid and a plurality of illumination modules (50), the illumination modules (50) of said plurality each having a planar form with first and second major surfaces (52, 54) and each comprising at least a first array (60) of semiconductor emitters (70), said emitters (70) positioned to emit from or through the first major surface (52), wherein said first array (60) of semiconductor emitters (70) comprises at least a first emitter (72) and a second emitter (74), the first emitter (72) capable of emitting at a first center wavelength and the second emitter (74) capable of emitting at a second center wavelength, said first and second center wavelengths differing from each other.
摘要翻译: 模块化光化学反应器系统包括多个流体模块(20),每个流体模块(20)各自具有i)中心平面过程流体层(30)和ii)用于容纳流动的热控制流体的两个外部平面热控制流体层(40) 照明模块(50),所述多个照明模块(50)具有平面形式,具有第一和第二主表面(52,54),并且每个包括至少半导体发射器(70)的第一阵列(60),所述 发射器(70)定位成从第一主表面(52)发射或穿过第一主表面(52),其中半导体发射器(70)的第一阵列(60)包括至少第一发射极(72)和第二发射极(74) 能够以第一中心波长发射的发射极(72)和能够以第二中心波长发射的第二发射极(74),所述第一和第二中心波长彼此不同。
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公开(公告)号:WO2003033117A1
公开(公告)日:2003-04-24
申请号:PCT/JP2002/010739
申请日:2002-10-16
IPC分类号: B01D53/86
CPC分类号: B01J21/18 , B01D53/504 , B01D53/8609 , B01J19/249 , B01J19/26 , B01J19/32 , B01J35/06 , B01J2219/00006 , B01J2219/2453 , B01J2219/2458 , B01J2219/2459 , B01J2219/247 , B01J2219/2483 , B01J2219/2496 , B01J2219/32206 , B01J2219/3221 , B01J2219/32213 , B01J2219/32227 , B01J2219/32268 , B01J2219/32275 , B01J2219/32433 , B01J2219/32466 , B01J2219/32491 , B32B2315/02 , C04B2237/385
摘要: A flue gas desulfurization apparatus, characterized in that an active carbon fiber layer (20) in a catalyst layer (6) comprises flat plate type active carbon fiber sheets and corrugated plate type active carbon fiber sheets which are laminated alternately and are arranged so that the passage for a fluid extends in the vertical direction, and the water for use in the formation of sulfuric acid is supplied to the active carbon fiber layer (20) in the catalyst layer (6) by utilizing capillary osmosis action, to thereby add a minimum amount of water for removing sulfur oxides (SO x ) uniformly to the active carbon fiber layer (20). The flue gas desulfurization apparatus allows the reduction of the amount of water required for removing sulfur oxides (SO x ).
摘要翻译: 一种烟道气脱硫装置,其特征在于,催化剂层(6)中的活性碳纤维层(20)包括交替层叠的平板型活性炭纤维片和波纹板状活性碳纤维片, 用于流体的通道在垂直方向上延伸,并且用于形成硫酸的水通过利用毛细管渗透作用被供应到催化剂层(6)中的活性碳纤维层(20),从而将最小 用于向活性碳纤维层(20)均匀地除去硫氧化物的水(SO x S x)。 烟气脱硫装置允许减少除去硫氧化物所需的水量(SO x Sb 2)。
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公开(公告)号:WO01096008A1
公开(公告)日:2001-12-20
申请号:PCT/CH2001/000343
申请日:2001-06-05
CPC分类号: B01J35/06 , B01J8/025 , B01J19/2465 , B01J19/249 , B01J19/2495 , B01J2208/00309 , B01J2208/00548 , B01J2219/00117 , B01J2219/00164 , B01J2219/2453 , B01J2219/2465 , B01J2219/2475 , B01J2219/2479 , B01J2219/2483 , B01J2219/2497 , C07C5/333 , Y02P20/52 , C07C11/06
摘要: The invention relates to a fixed bed (1a, 1b), especially a fixed bed with a catalyst, which has an anisotropic structure and which is located in a tubular part (21) of a reactor (20). A reaction fluid (30, 40) can flow through this reactor part (21) in the direction of its longitudinal extension. In the area containing the fixed bed, the reactor part has cross-sectional surfaces whose superficial contents are constant. In at least one direction, these cross-sectionals surfaces have inter-wall distances (d, a) that are considerably smaller than the longitudinal extension of the reactor part. The fixed bed structure comprises a plurality of microchannels in the direction of flow which to a large extent, are distributed homogeneously over the cross-sectional surface. The hydraulic diameters of the microchannels are less than 1 mm, so that the reaction fluid to be treated flows through the fixed bed structure in a laminar manner during a reaction.
摘要翻译: (1A 1B)固定床的,特别是固定床催化剂在反应器中(20)的管状部分(21)各向异性结构。 这通过反应液(30,40)在其纵向范围的方向上的反应器(21)的一部分流过。 在含固定床区域,它具有的横截面面积,其表面区域是恒定的。 该剖面具有至少在一个方向上壁间隙(D,A),其是比反应器部分的纵向延伸小得多。 固定床结构包括多个在其中基本上均匀地分布在横截面面积的流动方向微通道。 微通道的水力直径小于1毫米,使得流入进行反应,反应液被处理,固定床结构层。
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