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Stability investigation of micro-configured Pd-Ag membrane modules - Effect of operating temperature and pressure

机译:微型Pd-Ag膜组件的稳定性研究-工作温度和压力的影响

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The long-term stability over a period of up to 50 days has been reported for various designs of microstructured Pd77Ag23 membrane modules for H-2 production and purification. Even though microchannels provide sufficient mechanical support for moderate transmembrane pressure difference and temperatures, i.e., 4-5 bars and 400-450 degrees C, long-term operation under these operating conditions results in a large deformative settling of the Pd77Ag23 film into the microchannel support. This settling leads to microstructural changes and pore formation on the feed surface of the membrane film that ultimately results in membrane failure. For pressures above approximately 5 bars, the application of microchannel-supported modules is thus not feasible, and for that purpose a continuous porous stainless steel support is introduced that allows for a sufficient stabilisation of the thin Pd77Ag23 films. For such a porous stainless steel supported microchannel module, a hydrogen flux of 195.3 mL cm(-2) min(-1) is obtained at 450 degrees C and 5 bars feed pressure, corresponding to a permeability of 3.4.10(-8) mol m(-1) s(-1) Pa-0.5. During the complete operation of 1100 h at 450 degrees C, the module shows a very good stability up to the highest feed pressure applied of 15 bars. The N-2 leakage flux has remained below the detection limit of the equipment, 5 mu L cm(-2) min(-1), resulting in a minimum value for the H-2/N-2 permselectivity of 39.000 applying the pure H-2 flux value obtained at 5 bars. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:对于用于H-2生产和纯化的微结构化Pd77Ag23膜组件的各种设计,已经报道了长达50天的长期稳定性。即使微通道为中等的跨膜压差和温度(即4-5 bar和400-450摄氏度)提供了足够的机械支撑,但在这些操作条件下的长期操作仍会导致Pd77Ag23膜大量变形沉降到微通道支撑中。这种沉降导致膜的进料表面发生微观结构变化和孔形成,最终导致膜失效。因此,对于高于约5 bar的压力,使用微通道支撑的模块是不可行的,为此目的,引入了连续的多孔不锈钢支撑体,以使Pd77Ag23薄膜保持足够的稳定性。对于这样的多孔不锈钢支撑微通道模块,在450摄氏度和5巴进料压力下可获得195.3 mL cm(-2)min(-1)的氢通量,对应的渗透率为3.4.10(-8)摩尔m(-1)s(-1)Pa-0.5。在450摄氏度下1100小时的完整运行过程中,该模块在施加15巴的最高进料压力下显示出非常好的稳定性。 N-2泄漏通量一直保持在设备的检测极限以下,即5μL cm(-2)min(-1),使用纯净水后,H-2 / N-2的渗透选择性最小值为39.000。在5巴下获得H-2通量值。 Hydrogen Energy Publications,LLC版权所有(C)2014。由Elsevier Ltd.出版。保留所有权利。

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