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    • 4. 发明申请
    • CATALYTIC NANOPOROUS MEMBRANES
    • 催化纳米膜
    • US20100075827A1
    • 2010-03-25
    • US12610897
    • 2009-11-02
    • Michael J. PellinJohn N. HrynJeffrey W. Elam
    • Michael J. PellinJohn N. HrynJeffrey W. Elam
    • B01J35/10B01J21/04B01J23/22
    • C23C16/045B01J23/22B01J23/26B01J23/42B01J23/462B01J23/755B01J35/065B01J35/1057B01J35/1061B01J37/0226B01J37/0238B01J37/0244C23C16/18C23C16/402C23C16/403C23C16/405C23C16/407C23C16/45525C23C16/45555
    • A nanoporous catalytic membrane which displays several unique features Including pores which can go through the entire thickness of the membrane. The membrane has a higher catalytic and product selectivity than conventional catalysts. Anodic aluminum oxide (AAO) membranes serve as the catalyst substrate. This substrate is then subjected to Atomic Layer Deposition (ALD), which allows the controlled narrowing of the pores from 40 nm to 10 nm in the substrate by deposition of a preparatory material. Subsequent deposition of a catalytic layer on the inner surfaces of the pores reduces pore sizes to less than 10 nm and allows for a higher degree of reaction selectivity. The small pore sizes allow control over which molecules enter the pores, and the flow-through feature can allow for partial oxidation of reactant species as opposed to complete oxidation. A nanoporous separation membrane, produced by ALD is also provided for use in gaseous and liquid separations. The membrane has a high flow rate of material with 100% selectivity. Also provided is a method for producing a catalytic membrane having flow-through pores and discreet catalytic clusters adhering to the inside surfaces of the pores.
    • 纳米多孔催化膜,显示几个独特的特征包括可以穿过膜的整个厚度的孔。 该膜具有比常规催化剂更高的催化和产物选择性。 阳极氧化铝(AAO)膜用作催化剂底物。 然后将该衬底经受原子层沉积(ALD),其允许通过沉积预备材料在衬底中将孔的受控变窄从40nm至10nm。 随后在孔的内表面上沉积催化剂层将孔径减小到小于10nm,并允许较高程度的反应选择性。 小孔径允许控制哪些分子进入孔隙,而与完全氧化相反,流通特征可以允许反应物物质的部分氧化。 还提供由ALD生产的纳米多孔分离膜,用于气相和液体分离。 该膜具有高流速的材料,具有100%的选择性。 还提供了一种制备具有粘附到孔的内表面的流通孔和分散催化剂簇的催化膜的方法。
    • 5. 发明授权
    • Catalytic nanoporous membranes
    • 催化纳米多孔膜
    • US08518845B2
    • 2013-08-27
    • US12610897
    • 2009-11-02
    • Michael J. PellinJohn N. HrynJeffrey W. Elam
    • Michael J. PellinJohn N. HrynJeffrey W. Elam
    • B01J20/28B01J35/00B01J27/22B01J27/224B01J27/24B01J23/00B01J23/02B01J21/04B01J20/00
    • C23C16/045B01J23/22B01J23/26B01J23/42B01J23/462B01J23/755B01J35/065B01J35/1057B01J35/1061B01J37/0226B01J37/0238B01J37/0244C23C16/18C23C16/402C23C16/403C23C16/405C23C16/407C23C16/45525C23C16/45555
    • A nanoporous catalytic membrane which displays several unique features Including pores which can go through the entire thickness of the membrane. The membrane has a higher catalytic and product selectivity than conventional catalysts. Anodic aluminum oxide (AAO) membranes serve as the catalyst substrate. This substrate is then subjected to Atomic Layer Deposition (ALD), which allows the controlled narrowing of the pores from 40 nm to 10 nm in the substrate by deposition of a preparatory material. Subsequent deposition of a catalytic layer on the inner surfaces of the pores reduces pore sizes to less than 10 nm and allows for a higher degree of reaction selectivity. The small pore sizes allow control over which molecules enter the pores, and the flow-through feature can allow for partial oxidation of reactant species as opposed to complete oxidation. A nanoporous separation membrane, produced by ALD is also provided for use in gaseous and liquid separations. The membrane has a high flow rate of material with 100% selectivity. Also provided is a method for producing a catalytic membrane having flow-through pores and discreet catalytic clusters adhering to the inside surfaces of the pores.
    • 纳米多孔催化膜,显示几个独特的特征包括可以穿过膜的整个厚度的孔。 该膜具有比常规催化剂更高的催化和产物选择性。 阳极氧化铝(AAO)膜用作催化剂底物。 然后将该衬底经受原子层沉积(ALD),其允许通过沉积预备材料在衬底中将孔的受控变窄从40nm至10nm。 随后在孔的内表面上沉积催化剂层将孔径减小到小于10nm,并允许较高程度的反应选择性。 小孔径允许控制哪些分子进入孔隙,而与完全氧化相反,流通特征可以允许反应物物质的部分氧化。 还提供由ALD生产的纳米多孔分离膜,用于气相和液体分离。 该膜具有高流速的材料,具有100%的选择性。 还提供了一种制备具有粘附到孔的内表面的流通孔和分散催化剂簇的催化膜的方法。
    • 7. 发明授权
    • Method and apparatus for electrodialysis processing
    • 电渗析处理方法和装置
    • US06461491B1
    • 2002-10-08
    • US09589329
    • 2000-06-07
    • John N. HrynKandipati Sreenivasarao
    • John N. HrynKandipati Sreenivasarao
    • B01D6144
    • B01D61/52
    • An electrodialysis apparatus includes a stack of alternating cation and anion semi-permeable, ion-selective membranes disposed between a positive DC potential anode electrode and a negative DC potential cathode electrode. The cation and anion selective membranes can be selective for monovalent or multivalent ions and form compartments therebetween through alternate compartments of which flow concentrate and diluate solutions such that the concentrate and diluate solutions are separated from each other by the ion selective membranes. Due to the potential maintained across each of the compartments and the cation and anion selective membranes separating the compartments, cations and anions as well as water will migrate from the diluate solution to the concentrate solution. An anode electrode rinse solution is circulated through an outer most compartment adjacent to the anode electrode and a separate cathode electrode rinse solution is circulated through an outer most compartment adjacent to the cathode electrode.
    • 电渗析装置包括交替的阳离子和阴离子半透性的离子选择性膜的叠层,其布置在正的直流电位的阳极和负的直流电位的阴极之间。 阳离子和阴离子选择性膜可以是选择性的单价或多价离子,并通过其间隔的交替隔室形成隔室,其中流动浓缩物和稀释溶液使得浓缩物和稀释溶液通过离子选择性膜彼此分离。 由于分隔隔室的阳离子选择性膜和阳离子和阴离子以及水分离在每个隔室中并且从稀释溶液迁移至浓缩液。 阳极电极漂洗溶液循环通过与阳极电极相邻的最外层的隔室,并且单独的阴极电极漂洗溶液通过与阴极电极相邻的最外层隔室循环。