Abstract:
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, La 2 O 3 , CeO 2 , , ATiO 3 , AZrO 3 , AAl 2 O 4 , A 1 FeO 3 , A 1 MnO 3 , A 1 CoO 3 , A 1 NiO 3 , A 2 HfO 3 , A 3 CeO 3 , Li 2 ZrO 3 , Li 2 SiO 3 , Li 2 TiO 3 or a mixture thereof; wherein A is Mg, Ca, Sr or Ba; A 1 is La, Ca, Sr or Ba; A 2 is Ca, Sr or Ba; and A 3 is Sr or Ba.
Abstract translation:一种多孔膜,用于在高于约200℃的温度下从流体流中分离二氧化碳,其选择性高于努森扩散选择性。 多孔膜包含含有氧化铝,二氧化硅,氧化锆或稳定的氧化锆的多孔载体层; 包含氧化铝,二氧化硅,氧化锆或稳定的氧化锆的多孔分离层以及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 SUB 3,CeO 2,ATiO SUB, 3,AZrO 3,SUB 1,SUB 4,SUB 1,FEO 3, / SUB>,SUB1,SUB1,SUB1,SUB1,SUB1,SUB1,SUB1,SUB1,SUB1, > NiO <3>,<2> HfO <3>,3 <3> CeO <3>,Li 2 sub> ZrO <3>, 2 3 , 2 SUB> 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 2是Ca,Sr或Ba; 并且A 3是Sr或Ba。
Abstract:
A porous membrane structure is disclosed, which includes a porous substrate, a mesoporous, aluminum oxide layer disposed on the substrate; and a relatively thin, continuous, microporous barrier layer disposed on the mesoporous aluminum oxide layer, also formed from aluminum oxide. The membrane is capable of improving hydrogen selectivity within a gas stream, e.g., a synthesis gas composition. Membrane supports containing these structures are also described, as well as gas separation modules, and related processes. Power plants which incorporate the gas separation modules are also disclosed herein.
Abstract:
A membrane structure 10 is provided. The membrane structure includes a first layer 12 having a plurality of interconnected pores 14; and a second layer 16 disposed on the first layer. The second layer has a plurality of unconnected pores 18. Each of the unconnected pores is in fluid communication with at least one of the interconnected pores of the first layer. A method of making a membrane structure is provided. The method includes the steps of providing a first layer having a plurality of interconnected pores; and disposing a second layer on the first layer. Disposing a second layer includes depositing a conducting layer on the first layer; and anodizing the conducting layer to convert the conducting layer into a porous layer.
Abstract:
A membrane structure is provided. The membrane structure includes a first layer having a plurality of interconnected pores; and a second layer disposed on the first layer. The second layer has a plurality of unconnected pores. Each of the unconnected pores is in fluid communication with at least one of the interconnected pores of the first layer. A method of making a membrane structure is provided. The method includes the steps of providing a first layer having a plurality of interconnected pores; and disposing a second layer on the first layer. Disposing a second layer includes depositing a conducting layer on the first layer; and anodizing the conducting layer to convert the conducting layer into a porous layer.
Abstract:
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, La 2 O 3 , CeO 2 , , ATiO 3 , AZrO 3 , AAl 2 O 4 , A 1 FeO 3 , A 1 MnO 3 , A 1 CoO 3 , A 1 NiO 3 , A 2 HfO 3 , A 3 CeO 3 , Li 2 ZrO 3 , Li 2 SiO 3 , Li 2 TiO 3 or a mixture thereof; wherein A is Mg, Ca, Sr or Ba; A 1 is La, Ca, Sr or Ba; A 2 is Ca, Sr or Ba; and A 3 is Sr or Ba.
Abstract translation:选择性高于克氏扩散选择性的多孔膜,用于在高于约200℃的温度下从流体流中分离二氧化碳。 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,AT 1 O 3, 3个,3个,3个,3个,3个,3个,3个,3个,3个,3个,3个, / SUB,A 1,Mn 3 O 3,A 1,CO 3,A 1 SUP / NiO 3 3,HfO 3 3,Al 3 O 3,Li 3 O 3,Li 3 O 3, 二氧化锆3,Li 2 SiO 3,Li 2 O 2, 3或其混合物; 其中A是Mg,Ca,Sr或Ba; A 1是La,Ca,Sr或Ba; A SUP>是Ca,Sr或Ba; 和A 3是Sr或Ba。