JP2009006315A5 - - Google Patents

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JP2009006315A5
JP2009006315A5 JP2008133938A JP2008133938A JP2009006315A5 JP 2009006315 A5 JP2009006315 A5 JP 2009006315A5 JP 2008133938 A JP2008133938 A JP 2008133938A JP 2008133938 A JP2008133938 A JP 2008133938A JP 2009006315 A5 JP2009006315 A5 JP 2009006315A5
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semipermeable membrane
composite semipermeable
organic compound
producing
functional layer
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JP2008133938A
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JP5131028B2 (en
JP2009006315A (en
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上記目的を達成するための本発明は、微多孔性支持膜上での重縮合により架橋ポリアミド機能層を形成させた複合半透膜を、特定構造の化合物と接触処理することによってポリアミド分離機能層を改質し、膜性能の向上を図るものであり、以下のとおり特定される。
(1) 微多孔性支持膜上に、多官能アミンと多官能カルボン酸誘導体とを重縮合させてなるポリアミド分離機能層を形成させることにより複合半透膜を製造した後、ポリアミド分離機能層に、下記一般式(1)で示される構造を有する有機化合物またはその有機化合物と酸との塩を接触させる処理を行うことを特徴とする複合半透膜の製造方法。
In order to achieve the above object, the present invention provides a polyamide separation functional layer by subjecting a composite semipermeable membrane in which a crosslinked polyamide functional layer is formed by polycondensation on a microporous support membrane to a compound having a specific structure. To improve the membrane performance, and is specified as follows.
(1) After producing a composite semipermeable membrane by forming a polyamide separation functional layer obtained by polycondensation of a polyfunctional amine and a polyfunctional carboxylic acid derivative on a microporous support membrane, The manufacturing method of the composite semipermeable membrane characterized by performing the process which contacts the salt of the organic compound which has a structure shown by following General formula (1), or its organic compound, and an acid .

(式(1)中、Xは酸素原子、硫黄原子、NH基のいずれかを表し、R〜Rは水素原子、炭化水素基、オキシアルキル基のいずれかを表す。)
(2) 前記有機化合物の分子量が、59以上1000以下である上記(1)に記載の複合半透膜の製造方法。
(3) 前記有機化合物が、尿素、グアニジン及びチオ尿素から選ばれる少なくとも1種である(1)に記載の複合半透膜の製造方法。
(4) 25℃、pH=6.5、濃度0.2重量%の塩化ナトリウム水溶液を0.5MPaの操作圧力で透過させたときの塩化ナトリウム除去率が90%以上である複合半透膜の分離機能層を前記有機化合物と接触させる、上記(1)〜(3)の何れかに記載の複合半透膜の製造方法。
(In Formula (1), X represents an oxygen atom, a sulfur atom, or an NH group, and R 1 to R 4 represent any one of a hydrogen atom, a hydrocarbon group, and an oxyalkyl group.)
(2) The manufacturing method of the composite semipermeable membrane as described in said (1) whose molecular weight of the said organic compound is 59-1000.
(3) said organic compound is urea, guanidine and Chionyo fluorinated et al method for producing a composite semipermeable membrane according to at least one (1) to be selected.
(4) A composite semipermeable membrane having a sodium chloride removal rate of 90% or more when a sodium chloride aqueous solution of 25 ° C., pH = 6.5 and a concentration of 0.2% by weight is permeated at an operating pressure of 0.5 MPa. The method for producing a composite semipermeable membrane according to any one of (1) to (3), wherein the separation functional layer is brought into contact with the organic compound.

Claims (4)

微多孔性支持膜上に、多官能アミンと多官能酸ハロゲン化物とを重縮合させてなるポリアミド分離機能層を形成させることにより複合半透膜を製造した後、ポリアミド分離機能層に、下記一般式(1)で示される構造を有する有機化合物またはその有機化合物と酸との塩を接触させる処理を行うことを特徴とする複合半透膜の製造方法。
Figure 2009006315
(式(1)中、Xは酸素原子、硫黄原子、NH基のいずれかを表し、R〜Rは水素原子、炭化水素基、オキシアルキル基のいずれかを表す。)
After producing a composite semipermeable membrane by forming a polyamide separation functional layer formed by polycondensation of a polyfunctional amine and a polyfunctional acid halide on a microporous support membrane, The manufacturing method of the composite semipermeable membrane characterized by performing the process which contacts the salt of the organic compound which has a structure shown by Formula (1), or the organic compound, and an acid .
Figure 2009006315
(In Formula (1), X represents an oxygen atom, a sulfur atom, or an NH group, and R 1 to R 4 represent any one of a hydrogen atom, a hydrocarbon group, and an oxyalkyl group.)
前記有機化合物の分子量が、59以上1000以下である請求項1に記載の複合半透膜の製造方法。 The method for producing a composite semipermeable membrane according to claim 1, wherein the organic compound has a molecular weight of 59 or more and 1000 or less. 前記有機化合物が、尿素、グアニジン及びチオ尿素から選ばれる少なくとも1種である請求項1に記載の複合半透膜の製造方法。 The organic compound is urea, guanidine and Chionyo fluorinated et al method for producing a composite semipermeable membrane according to claim 1 is at least one selected. 25℃、pH=6.5、濃度0.2重量%の塩化ナトリウム水溶液を0.5MPaの操作圧力で透過させたときの塩化ナトリウム除去率が90%以上である複合半透膜の分離機能層を前記有機化合物と接触させる、請求項1〜3のいずれかに記載の複合半透膜の製造方法。 Separation functional layer of a composite semipermeable membrane having a sodium chloride removal rate of 90% or more when a sodium chloride aqueous solution of 25 ° C., pH = 6.5 and a concentration of 0.2% by weight is permeated at an operating pressure of 0.5 MPa. The manufacturing method of the composite semipermeable membrane in any one of Claims 1-3 which is made to contact with the said organic compound.
JP2008133938A 2007-05-30 2008-05-22 Manufacturing method of composite semipermeable membrane Expired - Fee Related JP5131028B2 (en)

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JP2008133938A JP5131028B2 (en) 2007-05-30 2008-05-22 Manufacturing method of composite semipermeable membrane

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JP2007142996 2007-05-30
JP2007142996 2007-05-30
JP2008133938A JP5131028B2 (en) 2007-05-30 2008-05-22 Manufacturing method of composite semipermeable membrane

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JP2009006315A5 true JP2009006315A5 (en) 2011-06-30
JP5131028B2 JP5131028B2 (en) 2013-01-30

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JP2009078218A (en) * 2007-09-26 2009-04-16 Toray Ind Inc Method of manufacturing composite semi-permeable membrane
CN102512982B (en) * 2012-01-11 2013-11-13 浙江理工大学 Antibacterial oxidation-resistant composite reverse osmosis membrane
US9211507B2 (en) 2012-11-21 2015-12-15 Lg Chem, Ltd. Water-treatment separating membrane of high flux having good chlorine resistance and method of manufacturing the same
CN104039430B (en) 2012-11-21 2016-06-01 Lg化学株式会社 There is high-throughput water treatment separatory membrane and its preparation method of good resistance to chlorine
CN104548945A (en) * 2013-10-23 2015-04-29 中国石油化工股份有限公司 After-treatment method for increasing flux of ultra-filtration membrane
CN103933878A (en) * 2014-04-25 2014-07-23 浙江理工大学 High-flux composite reverse osmosis membrane
TWI652106B (en) * 2017-04-19 2019-03-01 南韓商Lg化學股份有限公司 Water treatment membrane and preparation method thereof
CN114432901B (en) * 2020-11-02 2023-04-11 中国石油化工股份有限公司 Composite membrane with acid resistance and alkali resistance as well as preparation method and application thereof
CN114181389B (en) * 2021-05-31 2023-07-04 杭州聚合顺新材料股份有限公司 Antibacterial nylon 6 containing guanidine group and preparation method thereof

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JPS6354905A (en) * 1986-08-25 1988-03-09 Toray Ind Inc Production of semiosmosis composite membrane
CA1318091C (en) * 1987-01-15 1993-05-25 Filmtec Corporation Reverse osmosis membranes
US5755964A (en) * 1996-02-02 1998-05-26 The Dow Chemical Company Method of treating polyamide membranes to increase flux
JP2000334280A (en) * 1999-05-27 2000-12-05 Nitto Denko Corp Production of multiple reverse osmosis membrane
JP4525296B2 (en) * 2003-12-03 2010-08-18 東レ株式会社 Manufacturing method of composite semipermeable membrane
JP2006021094A (en) * 2004-07-07 2006-01-26 Toray Ind Inc Compound semi-permeable membrane and its manufacturing method

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