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    • 1. 发明申请
    • MEMBRANE STRUCTURE AND METHOD OF MAKING
    • 膜结构和制备方法
    • US20070125702A1
    • 2007-06-07
    • US11555506
    • 2006-11-01
    • Vidya RamaswamyJames RuudAnthony KuWilliam Huber
    • Vidya RamaswamyJames RuudAnthony KuWilliam Huber
    • B01D71/06
    • B01D67/0062B01D69/12B01D71/022B01J2219/00835B01J2219/00907Y10T428/249981
    • A membrane structure is provided. The membrane structure includes a polymer layer having a plurality of pores; and a ceramic layer disposed on the polymer layer. The ceramic layer has a plurality of substantially unconnected pores. Each of the substantially unconnected pores is in fluid communication with at least one of the pores of the polymer layer. A method of manufacturing a membrane structure is provided. The method includes the steps of providing a polymer layer having a plurality of pores; and disposing a ceramic layer on the polymer layer. Disposing a ceramic layer includes depositing a metal layer on the polymer layer; and anodizing the metal layer to convert the metal layer into a porous layer. At least one of the depositing step and the anodizing step is performed as a continuous process. Alternatively, at least one of the depositing and the anodizing step is performed as a batch process.
    • 提供膜结构。 膜结构包括具有多个孔的聚合物层; 以及设置在聚合物层上的陶瓷层。 陶瓷层具有多个基本上未连接的孔。 每个基本上未连接的孔与聚合物层的至少一个孔流体连通。 提供一种制造膜结构的方法。 该方法包括提供具有多个孔的聚合物层的步骤; 并在聚合物层上设置陶瓷层。 布置陶瓷层包括在聚合物层上沉积金属层; 并阳极氧化金属层以将金属层转化为多孔层。 沉积步骤和阳极氧化步骤中的至少一个作为连续工艺进行。 或者,沉积和阳极化步骤中的至少一个作为分批处理进行。
    • 2. 发明申请
    • Functionalized inorganic membranes for gas separation
    • 用于气体分离的官能化无机膜
    • US20070068382A1
    • 2007-03-29
    • US11263165
    • 2005-10-31
    • Anthony KuJames RuudJennifer MolaisonLouis SchickVidya Ramaswamy
    • Anthony KuJames RuudJennifer MolaisonLouis SchickVidya Ramaswamy
    • B01D53/22
    • B01D71/024B01D53/228B01D69/12B01D2323/08Y02C10/10
    • A porous membrane for separation of carbon dioxide from a fluid stream at a temperature higher than about 200° C. with selectivity higher than Knudsen diffusion selectivity. The porous membrane comprises a porous support layer comprising alumina, silica, zirconia or stabilized zirconia; a porous separation layer comprising alumina, silica, zirconia or stabilized zirconia, and a functional layer comprising a ceramic oxide contactable with the fluid stream to preferentially transport carbon dioxide. In particular, the functional layer may be MgO, CaO, SrO, BaO, La2O3, CeO2, ATiO3, AZrO3, AAl2O4, A1FeO3, A1MnO3, A1CoO3, A1NiO3, A2HfO3, A3CeO3, Li2ZrO3, Li2SiO3, Li2TiO3 or a mixture thereof; wherein A is Mg, Ca, Sr or Ba; A1 is La, Ca, Sr or Ba; A2 is Ca, Sr or Ba; and A3 is Sr or Ba.
    • 一种用于在高于约200℃的温度下将二氧化碳与流体物流分离的多孔膜,选择性高于克努森扩散选择性。 多孔膜包括多孔支撑层,包括氧化铝,二氧化硅,氧化锆或稳定的氧化锆; 包括氧化铝,二氧化硅,氧化锆或稳定的氧化锆的多孔分离层和包含可与流体流接触以优先输送二氧化碳的陶瓷氧化物的功能层。 特别地,功能层可以是MgO,CaO,SrO,BaO,La 2 O 3,CeO 2,ATiO 3 AZrO 3,AA 1,2 O 4,A 1,Fe 3,3, A 1,...,N 2,A 1,...,...,...,...,... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... ... NiO 3,3O 3,3O 3,3%,3%,3%,3%,3% SUB 2 2 ZrO 3 3,Li 2 SiO 3 3,Li 2 TiO 3 或其混合物; 其中A是Mg,Ca,Sr或Ba; A 1是La,Ca,Sr或Ba; A 是Ca,Sr或Ba; 和A 3是Sr或Ba。