欢迎登录材料期刊网

材料期刊网

高级检索

利用钯膜分离氢是高纯或超纯氢气生产的主要方式,然而,钯膜表面缺陷是影响氢分离纯度的主要因素.本文选择NaA分子筛和γ-Al2O3两种缺陷填充材料对初镀后的钯膜表面缺陷进行修饰,发现两种材料修饰后钯膜透氮量分别下降了57和2倍,NaA分子筛材料修饰后钯膜的透氮量为未修饰钯膜的1/2 500.经过补镀和活化后,在相同钯膜厚度(2.5μm)条件下,3种钯膜透氮量分别为1.91×10-3、6.12×10-4和4.89×10-3m3/(h·m2·MPa).不同修饰材料修饰的钯膜的氢氮分离因子顺序为NaA分子筛>γ-Al2O3>无修饰,说明通过修饰钯膜缺陷的方法可提高钯膜的氢分离选择性,且用NaA分子筛材料要优于γ-Al2 O3材料,因为NaA分子筛在缺陷中可根据缺陷形状原位生长,更能有效填补缺陷.NaA分子筛材料修饰后的钯膜经过20次300~400℃以及0.1~1.0 MPa的温度和压力循环仍保持性能不变,具有较高的稳定性.

参考文献

[1] Nong Xu;Shinkun Ryi;Anwu Li .IMPROVED PRE-TREATMENT OF POROUS STAINLESS STEEL SUBSTRATE FOR PREPARATION OF PD-BASED COMPOSITE MEMBRANE[J].The Canadian Journal of Chemical Engineering,2013(10):1695-1701.
[2] Carolina A. Cornaglia;Silvano Tosti;Mirko Sansovini.Novel catalyst for the WGS reaction in a Pd-membrane reactor[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2013:278-286.
[3] Garcia-Garcia F R;Soria M A;Mateos-Pedrero C et al.Dry reforming of methane using Pd-based membrane reactors fabricated from different substrates[J].Journal of Membrane Science,2013,435:218-225.
[4] Kyung-Ran Hwang;Sung-Wook Lee;Shin-Kun Ryi.Water-gas shift reaction in a plate-type Pd-membrane reactor over a nickel metal catalyst[J].Fuel Processing Technology,2013:133-140.
[5] Wei-Hsin Chen;Ming-Hsien Hsia;Yu-Li Lin;Yen-Hsun Chi;Chang-Chung Yang .Hydrogen permeation and recovery from H_2-N_2 gas mixtures by Pd membranes with high permeance[J].International journal of hydrogen energy,2013(34):14730-14742.
[6] Tanczyk Marek;Gosiewski Krzysztof .Separation properties of membranes in membrane reactors for conversion of CO with simultaneous H2 recovery[J].Przemysl Chemiczny,2012,91(12):2419-2421.
[7] 李安武,熊国兴,R.Hughes.致密钯膜中裂缺的修补[J].中国科学B辑,1999(02):169-173.
[8] Uemiya S;Sato N;Ando H et al.Separation of hydrogen through palladium thin film supported on a porous glass tube[J].Journal of Membrane Science,1991,56:303-313.
[9] 胡小娟,魏娟,黄彦.Pd(OH)2胶体预处理及化学镀法修补复合Pd膜[J].南京工业大学学报(自然科学版),2011(03):43-48.
[10] Li Anwu;Liang Weiqiang;Hughes Ronald .Repair of a Pd/α-Al2 O3 composite membrane containing defects[J].Separation and Purification Technology,1999,15(2):113-119.
[11] Li Anwu;Liang Weiqiang;Hughes Ronald .Fabrication of defect-free Pd/γ-Al2 O3 composite membranes for hydrogen separation[J].THIN SOLID FILMS,1999,359(1/2):106-112.
[12] 徐恒泳;袁立祥 .一种修饰补钯及钯合金复合膜缺陷的方法[P].中国,申请号:200810104368.7,2009-10-21.
[13] Zeng Gaofeng;Goldbach Andreas;Xu Hengyong .Defect sealing in Pd membranes via point-plating[J].Journal of Membrane Science,2009,328:6-10.
[14] Bosko M L;Múnera J F;Lombardo E A et al.Dry reforming of methane in membrane reactors using Pd and Pd Ag composite membranes on a NaA zeolite modified porous stainless steel support[J].Journal of Membrane Science,2010,364(1/2):17-26.
[15] 唐春华,邵炜,徐恒泳.超薄金属钯复合膜表面缺陷修饰的研究[J].天然气化工,2009(01):10-16.
[16] 徐恒泳;侯守福;李文钊 等.一种复合金属钯膜或合金钯膜及其制备方法[P].中国,专利号:200410021025.6,2005-07-20.
[17] 徐恒泳;唐春华;李春林 等.一种高透氢选择性金属钯复合膜的制备方法[P].中国,专利号:200810013153.4,2014-010-01.
[18] Jianhua Tong;Yasuyuki matsumura .Thin Pd membrane prepared on macroporous stainless steel tube filter by an in-situ multi-dimensional plating mechanism[J].Chemical communications,2004(21):2460-2461.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%