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Performance of Pd-Based Membranes and Effects of Various Gas Mixtures on H 2 Permeation

机译:钯基膜的性能以及各种气体混合物对H 2渗透的影响

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H 2 permeation and separation properties of two Pd-based composite membranes were evaluated and compared at 400 °C and at a pressure range of 150 kPa to 600 kPa. One membrane was characterized by an approximately 8 μm-thick palladium (Pd)-gold (Au) layer deposited on an asymmetric microporous Al 2 O 3 substrate; the other membrane consisted of an approximately 11 μm-thick pure palladium layer deposited on a yttria-stabilized zirconia (YSZ) support. At 400 °C and with a trans-membrane pressure of 50 kPa, the membranes showed a H 2 permeance of 8.42 × 10 ?4 mol/m 2 ·s·Pa 0.5 and 2.54 × 10 ?5 mol/m 2 ·s·Pa 0.7 for Pd-Au and Pd membranes, respectively. Pd-Au membrane showed infinite ideal selectivity to H 2 with respect to He and Ar at 400 °C and a trans-membrane pressure of 50 kPa, while the ideal selectivities for the Pd membrane under the same operating conditions were much lower. Furthermore, the permeation tests for ternary and quaternary mixtures of H 2 , CO, CO 2 , CH 4 , and H 2 O were conducted on the Pd/YSZ membrane. The H 2 permeating flux decreased at the conclusion of the permeation tests for all mixtures. This decline however, was not permanent, i.e., H 2 permeation was restored to its initial value after treating the membrane with H 2 for a maximum of 7 h. The effects of gas hourly space velocity (GHSV) and the steam-to-carbon (S/C) ratio on H 2 permeation were also investigated using simulated steam methane reforming mixtures. It was found that H 2 permeation is highest at the greatest GHSV, due to a decline in the concentration polarization effect. Variations in S/C ratio however, showed no significant effect on the H 2 permeation. The permeation characteristics for the Pd/YSZ membrane were also investigated at temperatures ranging from 350 to 400 °C. The pre-exponential factor and apparent activation energy were found to be 5.66 × 10 ?4 mol/m 2 ·s·Pa 0.7 and 12.8 kJ/mol, respectively. Scanning Electron Microscope (SEM) and X-ray diffraction (XRD) analyses were performed on both pristine and used membranes, and no strong evidence of the formation of Pd-O or any other undesirable phases was observed.
机译:在400℃和150kPa至600kPa的压力范围内,评估并比较了两种Pd基复合膜的H 2渗透和分离性能。一种膜的特征是沉积在不对称微孔Al 2 O 3衬底上的约8μm厚的钯(Pd)-金(Au)层;另一膜由沉积在氧化钇稳定的氧化锆(YSZ)载体上的约11μm厚的纯钯层组成。在400°C且跨膜压力为50 kPa时,膜的H 2渗透率分别为8.42×10?4 mol / m 2·s·Pa·0.5和2.54×10?5 mol / m 2·s·Pa· Pd-Au和Pd膜的Pa分别为0.7。 Pd-Au膜在400°C和50 kPa的跨膜压力下对He和Ar表现出对H 2的无限理想选择,而在相同操作条件下Pd膜的理想选择性则低得多。此外,在Pd / YSZ膜上进行了H 2,CO,CO 2,CH 4和H 2 O的三元和四元混合物的渗透测试。在所有混合物的渗透测试结束时,H 2渗透通量均降低。然而,这种下降不是永久的,即,在用H 2处理膜最多7小时后,H 2的渗透恢复到其初始值。还使用模拟的蒸汽甲烷重整混合物研究了气体时空速(GHSV)和蒸汽碳比(S / C)对H 2渗透的影响。已经发现,由于浓度极化效应的下降,H 2的渗透在最大的GHSV处最高。但是,S / C比的变化对H 2的渗透没有显着影响。 Pd / YSZ膜的渗透特性也在350至400°C的温度范围内进行了研究。发现前指数因子和表观活化能分别为5.66×10 -4 mol / m 2·s·Pa 0.7和12.8 kJ / mol。在原始膜和用过的膜上均进行了扫描电子显微镜(SEM)和X射线衍射(XRD)分析,未观察到形成Pd-O或任何其他不良相的有力证据。

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