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    • 2. 发明申请
    • SOLVENT-RESISTANT ASYMMETRIC HOLLOW FIBER GAS SEPARATION MEMBRANE, AND METHOD FOR PRODUCTION THEREOF
    • 耐溶剂不对称中空纤维气体分离膜及其生产方法
    • US20110048229A1
    • 2011-03-03
    • US12863125
    • 2009-01-19
    • Harutoshi HoshinoTomonori KanougiToshimune YoshinagaYoji KaseKenji Fukunaga
    • Harutoshi HoshinoTomonori KanougiToshimune YoshinagaYoji KaseKenji Fukunaga
    • B01D53/22C08J9/00
    • B01D69/08B01D53/228B01D71/40B01D71/80B01D2323/08B01D2325/24B01D2325/30C08G73/1039C08G73/1042C08G73/1064C08G73/1067D01F6/74
    • An asymmetric hollow fiber gas separation membrane obtained by subjecting an asymmetric hollow fiber polyimide membrane to a heat treatment having a maximum temperature of from 350 to 450° C., wherein the asymmetric hollow fiber polyimide membrane is formed with a polyimide essentially having a repeating unit represented by a general formula (1); is excellent in a solvent resistance and a thermal stability, and as well has such a mechanical strength that a tensile elongation at break is not less than 10% as a hollow fiber membrane. In the general formula (1), 20 to 80 mol % of A is a tetravalent unit based on a biphenyl structure represented by formula (2), 20 to 80 mol % of A is a tetravalent unit based on a diphenylhexafluoropropane structure represented by formula (3), and 0 to 30 mol % of A is a tetravalent unit based on a phenyl structure represented by formula (4); and in the general formula (1), 30 to 70 mol % of R is a divalent unit represented by formula (5) and/or formula (6), and 30 to 70 mol % of R is a divalent unit having one or two other aromatic rings than formula (5) or (6), wherein, R1 and R2 are a hydrogen atom or an organic group, and n is 0, 1 or 2, wherein, R1 and R2 are a hydrogen atom or an organic group, X is —CH2— or —CO—, and n is 0, 1 or 2.
    • 通过使不对称中空纤维聚酰亚胺膜进行350〜450℃的最高温度的热处理而得到的不对称中空纤维气体分离膜,其中,所述不对称中空纤维聚酰亚胺膜形成有基本上具有重复单元的聚酰亚胺 由通式(1)表示; 耐溶剂性和热稳定性优异,作为中空纤维膜,具有拉伸断裂伸长率为10%以上的机械强度。 在通式(1)中,A为20〜80摩尔%,为基于式(2)所示的联苯结构的四价单元,A为20〜80摩尔%,基于式(2)表示的二苯基六氟丙烷结构的四价单元 (3)表示,0〜30摩尔%的A为基于式(4)表示的苯基结构的四价单元。 在通式(1)中,R为作为式(5)和/或式(6)所示的二价单元的30〜70摩尔%,R为30〜70摩尔%,为1或2个 (5)或(6)中的其它芳环,其中R1和R2是氢原子或有机基团,n是0,1或2,其中R1和R2是氢原子或有机基团, X是-CH 2 - 或-CO-,n是0,1或2。
    • 3. 发明授权
    • Hollow-fiber element for organic-vapor separation
    • 用于有机蒸气分离的中空纤维元件
    • US09248408B2
    • 2016-02-02
    • US13262158
    • 2010-03-31
    • Tomonori KanougiYuma IrisaKenji Fukunaga
    • Tomonori KanougiYuma IrisaKenji Fukunaga
    • B01D63/02
    • B01D63/02B01D63/022B01D63/023B01D2313/08
    • In a hollow fiber element constituting a separation membrane module for separating an organic vapor, at least one end part of a fiber bundle consisting of multiple hollow fiber membranes having a selective permeability is fixed and bound with a tube sheet formed by a cured material, in which an epoxy composition (A) has been cured by using a hardener (B). A glass transition temperature of said cured material is not less than 160° C., a minimum elongation at break thereof is not less than 7.0%, and an elution ratio thereof is less than 5%. For this reason, the hollow fiber element has enough endurance to retain a gas-tightness of an internal space of the hollow fiber membrane and an external space of the hollow fiber membrane even in use under organic vapor with an elevated temperature and high pressure.
    • 在构成用于分离有机蒸气的分离膜组件的中空纤维元件中,由具有选择性渗透性的多个中空纤维膜组成的纤维束的至少一个端部固定并与由固化材料形成的管板结合, 其中环氧组合物(A)已经通过使用硬化剂(B)固化。 所述固化材料的玻璃化转变温度不低于160℃,最小断裂伸长率不小于7.0%,洗脱比小于5%。 因此,中空纤维元件具有足够的耐久性,即使在高温高压下在有机蒸气下使用也能够保持中空纤维膜的内部空间的气密性和中空纤维膜的外部空间。
    • 4. 发明授权
    • Hollow-fiber element for organic-vapor separation
    • 用于有机蒸气分离的中空纤维元件
    • US08388733B2
    • 2013-03-05
    • US12679883
    • 2008-09-29
    • Shoichi YamaokaShigekazu OkamuraMasao KikuchiTomonori KanougiYuma Irisa
    • Shoichi YamaokaShigekazu OkamuraMasao KikuchiTomonori KanougiYuma Irisa
    • B01D53/22
    • B01D63/023B01D53/22B01D61/36B01D63/022B01D2257/708C08K5/18C08L63/00
    • A hollow fiber element constituting a separation membrane module for separating an organic vapor is disclosed. At least one end part of a fiber bundle consisting of multiple hollow fiber membranes having a selective permeability is fixed and bound with a tube sheet formed by a cured material of an epoxy resin composition. Herein, a resin component of the epoxy resin composition contains an epoxy compound (A) represented by the following formula (1), an epoxy compound (B) represented by the following formula (2) and an aromatic amine compound (C), and wherein the epoxy compound (A) and the epoxy compound (B) are blended at a proportion in a range from 90:10 to 60:40 by weight; wherein R denotes alkyl group having 1 to 3 carbon atoms or hydrogen atom. The tube sheet has enough endurance to retain a gas-tightness of an internal space of the hollow fiber membrane and an external space of the hollow fiber membrane even in use under organic vapor with an elevated temperature and high pressure, and is suitably moldable in a stationary state as well.
    • 公开了构成用于分离有机蒸气的分离膜组件的中空纤维元件。 由具有选择性渗透性的多个中空纤维膜组成的纤维束的至少一个端部与由环氧树脂组合物的固化材料形成的管板固定并结合。 这里,环氧树脂组合物的树脂成分含有下述式(1)表示的环氧化合物(A),下述式(2)表示的环氧化合物(B)和芳香族胺化合物(C),以及 其中环氧化合物(A)和环氧化合物(B)以90:10至60:40的比例混合; 其中R表示具有1至3个碳原子的烷基或氢原子。 管板具有足够的耐久性,即使在高温高压下在有机蒸汽下使用也能够保持中空纤维膜的内部空间的气密性和中空纤维膜的外部空间,并且可适当地模制在 固定状态也是如此。
    • 9. 发明授权
    • Solvent-resistant asymmetric hollow fiber gas separation membrane, and method for production thereof
    • 耐溶剂型不对称中空纤维气体分离膜及其制造方法
    • US08580012B2
    • 2013-11-12
    • US12863125
    • 2009-01-19
    • Harutoshi HoshinoTomonori KanougiToshimune YoshinagaYoji KaseKenji Fukunaga
    • Harutoshi HoshinoTomonori KanougiToshimune YoshinagaYoji KaseKenji Fukunaga
    • B01D53/22B01D71/64
    • B01D69/08B01D53/228B01D71/40B01D71/80B01D2323/08B01D2325/24B01D2325/30C08G73/1039C08G73/1042C08G73/1064C08G73/1067D01F6/74
    • An asymmetric hollow fiber gas separation membrane obtained by subjecting an asymmetric hollow fiber polyimide membrane to a heat treatment having a maximum temperature of from 350 to 450° C., wherein the asymmetric hollow fiber polyimide membrane is formed with a polyimide essentially having a repeating unit represented by a general formula (1); is excellent in a solvent resistance and a thermal stability, and as well has such a mechanical strength that a tensile elongation at break is not less than 10% as a hollow fiber membrane. In the general formula (1), 20 to 80 mol % of A is a tetravalent unit based on a biphenyl structure represented by formula (2), 20 to 80 mol % of A is a tetravalent unit based on a diphenylhexafluoropropane structure represented by formula (3), and 0 to 30 mol % of A is a tetravalent unit based on a phenyl structure represented by formula (4); and in the general formula (1), 30 to 70 mol % of R is a divalent unit represented by formula (5) and/or formula (6), and 30 to 70 mol % of R is a divalent unit having one or two other aromatic rings than formula (5) or (6), wherein, R1 and R2 are a hydrogen atom or an organic group, and n is 0, 1 or 2, wherein, R1 and R2 are a hydrogen atom or an organic group, X is —CH2— or —CO—, and n is 0, 1 or 2.
    • 通过使不对称中空纤维聚酰亚胺膜进行350〜450℃的最高温度的热处理而得到的不对称中空纤维气体分离膜,其中,所述不对称中空纤维聚酰亚胺膜形成有基本上具有重复单元的聚酰亚胺 由通式(1)表示; 耐溶剂性和热稳定性优异,作为中空纤维膜,具有拉伸断裂伸长率为10%以上的机械强度。 在通式(1)中,A为20〜80摩尔%,为基于式(2)所示的联苯结构的四价单元,A为20〜80摩尔%,基于式(2)表示的二苯基六氟丙烷结构的四价单元 (3)表示,0〜30摩尔%的A为基于式(4)表示的苯基结构的四价单元。 在通式(1)中,R为作为式(5)和/或式(6)所示的二价单元的30〜70摩尔%,R为30〜70摩尔%,为1或2个 (5)或(6)中的其它芳环,其中R1和R2是氢原子或有机基团,n是0,1或2,其中R1和R2是氢原子或有机基团, X是-CH 2 - 或-CO-,n是0,1或2。
    • 10. 发明申请
    • HOLLOW-FIBER ELEMENT FOR ORGANIC-VAPOR SEPARATION
    • 有机蒸汽分离器的中空元件
    • US20120031831A1
    • 2012-02-09
    • US13262158
    • 2010-03-31
    • Tomonori KanougiYuma IrisaKenji Fukunaga
    • Tomonori KanougiYuma IrisaKenji Fukunaga
    • B01D63/04
    • B01D63/02B01D63/022B01D63/023B01D2313/08
    • In a hollow fiber element constituting a separation membrane module for separating an organic vapor, at least one end part of a fiber bundle consisting of multiple hollow fiber membranes having a selective permeability is fixed and bound with a tube sheet formed by a cured material, in which an epoxy composition (A) has been cured by using a hardener (B). A glass transition temperature of said cured material is not less than 160° C., a minimum elongation at break thereof is not less than 7.0%, and an elution ratio thereof is less than 5%. For this reason, the hollow fiber element has enough endurance to retain a gas-tightness of an internal space of the hollow fiber membrane and an external space of the hollow fiber membrane even in use under organic vapor with an elevated temperature and high pressure.
    • 在构成用于分离有机蒸气的分离膜组件的中空纤维元件中,由具有选择性渗透性的多个中空纤维膜组成的纤维束的至少一个端部被固化并与由固化材料形成的管板结合, 其中环氧组合物(A)已经通过使用硬化剂(B)固化。 所述固化材料的玻璃化转变温度不低于160℃,最小断裂伸长率不小于7.0%,洗脱比小于5%。 因此,中空纤维元件具有足够的耐久性,即使在高温高压下在有机蒸气下使用也能够保持中空纤维膜的内部空间的气密性和中空纤维膜的外部空间。