JP2008036574A5 - - Google Patents

Download PDF

Info

Publication number
JP2008036574A5
JP2008036574A5 JP2006216910A JP2006216910A JP2008036574A5 JP 2008036574 A5 JP2008036574 A5 JP 2008036574A5 JP 2006216910 A JP2006216910 A JP 2006216910A JP 2006216910 A JP2006216910 A JP 2006216910A JP 2008036574 A5 JP2008036574 A5 JP 2008036574A5
Authority
JP
Japan
Prior art keywords
membrane
water treatment
less
filtration
treatment method
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2006216910A
Other languages
Japanese (ja)
Other versions
JP2008036574A (en
Filing date
Publication date
Application filed filed Critical
Priority to JP2006216910A priority Critical patent/JP2008036574A/en
Priority claimed from JP2006216910A external-priority patent/JP2008036574A/en
Publication of JP2008036574A publication Critical patent/JP2008036574A/en
Publication of JP2008036574A5 publication Critical patent/JP2008036574A5/ja
Pending legal-status Critical Current

Links

Description

すなわち本発明は、
(1)ポリフッ化ビニリデン系樹脂からなる分離膜をろ過膜として用いてなる水処理用膜モジュールにおいて、分離膜が、セルロースエステルを含有してなる三次元網目構造と球状構造の両方を有し、かつ、ろ過抵抗上昇度Aが2×1012/m以上、逆洗回復性が50%以上、ろ過抵抗上昇度Bが2×1012/m以下、かつ、初期ろ過抵抗が1×1012/m以下の特性を有する膜である膜モジュール。
(2)上記(1)記載の膜モジュールにおいて、使用される分離膜の孔径が0.1μm以下である膜モジュール。
(3)上記(1)又は(2)記載の膜モジュールにおいて、使用される分離膜の開孔率が20%未満である膜モジュール。
(4)上記(3)に記載の膜モジュールを具備する膜ろ過装置を用い、物理洗浄を定期的に行いながら水処理を行ない透過水を製造する水処理方法。
(5)上記(4)に記載の水処理方法において、物理洗浄に逆流洗浄である水処理方法。
(6)上記(4)に記載の水処理方法において、物理洗浄を行う間隔が10分毎以上60分毎以下である水処理方法。
(7)上記(5)に記載の水処理方法において、使用される分離膜が中空糸膜である水処理方法。
からなるものである。
That is, the present invention
(1) In a membrane module for water treatment using a separation membrane made of polyvinylidene fluoride resin as a filtration membrane, the separation membrane has both a three-dimensional network structure containing a cellulose ester and a spherical structure, In addition, the filtration resistance increase A is 2 × 10 12 / m 2 or more, the backwash recovery is 50% or more, the filtration resistance increase B is 2 × 10 12 / m 2 or less, and the initial filtration resistance is 1 × 10. A membrane module which is a membrane having a characteristic of 12 / m or less.
(2) The membrane module according to (1), wherein the pore size of the separation membrane used is 0.1 μm or less.
(3) The membrane module according to the above (1) or (2), wherein the separation membrane used has a porosity of less than 20%.
(4) A water treatment method for producing permeated water by using a membrane filtration apparatus comprising the membrane module according to (3) above and performing water treatment while periodically performing physical cleaning.
(5) The water treatment method according to (4), wherein the physical washing is back-flow washing.
(6) The water treatment method according to (4), wherein the physical cleaning interval is 10 minutes or more and 60 minutes or less.
(7) The water treatment method according to (5), wherein the separation membrane used is a hollow fiber membrane.
It consists of

フッ素樹脂系高分子の場合の貧溶媒としては、シクロヘキサノン、イソホロン、γ−ブチロラクトン、メチルイソアミルケトン、フタル酸ジメチル、プロピレングリコールメチルエーテル、プロピレンカーボネート、ジアセトンアルコール、グリセロールトリアセテート等の中鎖長のアルキルケトン、エステル、グリコールエステルおよび有機カーボネート等およびそれらの混合溶媒が挙げられる。非溶媒と貧溶媒の混合溶媒であっても、上記貧溶媒の定義を満足するものは、貧溶媒として扱う。また、良溶媒としては、N−メチル−2−ピロリドン、ジメチルスルホキシド、ジメチルアセトアミド、ジメチルホルムアミド、メチルエチルケトン、アセトン、テトラヒドロフラン、テトラメチル尿素、リン酸トリメチル等の低級アルキルケトン、エステル、アミド等およびそれらの混合溶媒が挙げられる。さらに、非溶媒としては、水、ヘキサン、ペンタン、ベンゼン、トルエン、メタノール、エタノール、四塩化炭素、o−ジクロルベンゼン、トリクロルエチレン、エチレングリコール、ジエチレングリコール、トリエチレングリコール、プロピレングリコール、ブチレングリコール、ペンタンジオール、ヘキサンジオール、低分子量のポリエチレングリコール等の脂肪族炭化水素、芳香族炭化水素、脂肪族多価アルコール、芳香族多価アルコール、塩素化炭化水素、またはその他の塩素化有機液体およびそれらの混合溶媒が挙げられる。
Examples of poor solvents for fluoropolymers include cyclohexanone, isophorone, γ-butyrolactone, methyl isoamyl ketone, dimethyl phthalate, propylene glycol methyl ether, propylene carbonate, diacetone alcohol, and glycerol triacetate. Examples include ketones, esters, glycol esters and organic carbonates, and mixed solvents thereof. Even if it is a mixed solvent of a non-solvent and a poor solvent, what satisfies the definition of the poor solvent is treated as a poor solvent. As the good solvent, N- methyl-2-pyrrolidone, dimethyl sulfoxide, dimethylacetamide, dimethylformamide, methyl ethyl ketone, acetone, tetrahydrofuran, tetramethylurea, lower alkyl ketones trimethyl phosphate, etc., esters and amides and their The mixed solvent is mentioned. Further, non-solvents include water, hexane, pentane, benzene, toluene, methanol, ethanol, carbon tetrachloride, o-dichlorobenzene, trichloroethylene, ethylene glycol, diethylene glycol, triethylene glycol, propylene glycol, butylene glycol, pentane. Aliphatic hydrocarbons such as diol, hexanediol, low molecular weight polyethylene glycol, aromatic hydrocarbons, aliphatic polyhydric alcohols, aromatic polyhydric alcohols, chlorinated hydrocarbons, or other chlorinated organic liquids and mixtures thereof A solvent is mentioned.

圧力計を設置した10Lのステンレス製加圧タンクADVANTEC PRESSURE VESSEL DV−10に原水を入れ、同様に圧力計を設置した40Lのステンレス製加圧タンクADVANTEC PRESSURE VESSEL DV−40に和光純薬製蒸留水を入れた。それぞれのタンクには水の流出口に2方コックを接続した。原水には、フミン酸(和光純薬製)30mgと塩化カルシウム(ナカライテスク製 一級)250mgを和光純薬蒸留水10Lに溶解させたものを用いた。
Raw water is put into a 10L stainless steel pressurized tank ADVANTEC PRESURE VES SEL DV-10 with a pressure gauge installed, and a 40L stainless steel pressurized tank ADVANTEC PRESSURE VES SEL DV-40 with a pressure gauge installed is made by Wako Pure Chemical Industries, Ltd. Distilled water was added. Each tank was connected to a two-way cock at the water outlet. As raw water, 30 mg of humic acid (manufactured by Wako Pure Chemical Industries) and 250 mg of calcium chloride (manufactured by Nacalai Tesque) were dissolved in 10 L of Wako Pure Chemical distilled water.

Figure 2008036574
Figure 2008036574

Claims (7)

ポリフッ化ビニリデン系樹脂からなる分離膜をろ過膜として用いてなる水処理用膜モジュールにおいて、分離膜が、セルロースエステルを含有してなる三次元網目構造と球状構造の両方を有し、かつ、ろ過抵抗上昇度Aが2×1012/m以上、逆洗回復性が50%以上、ろ過抵抗上昇度Bが2×1012/m以下、かつ、初期ろ過抵抗が1×1012/m以下の特性を有する膜であることを特徴とする膜モジュール。 In a membrane module for water treatment using a separation membrane made of polyvinylidene fluoride resin as a filtration membrane, the separation membrane has both a three-dimensional network structure containing a cellulose ester and a spherical structure, and filtration. Resistance increase A is 2 × 10 12 / m 2 or more, backwash recovery is 50% or more, filtration resistance increase B is 2 × 10 12 / m 2 or less, and initial filtration resistance is 1 × 10 12 / m. A membrane module characterized by being a membrane having the following characteristics. 請求項1記載の膜モジュールにおいて、使用される分離膜の孔径が0.1μm以下である膜モジュール。 The membrane module according to claim 1, wherein the separation membrane used has a pore diameter of 0.1 µm or less. 請求項1又は2記載の膜モジュールにおいて、使用される分離膜の開孔率が20%未満である膜モジュール。 The membrane module according to claim 1 or 2, wherein the separation membrane used has a porosity of less than 20%. 請求項3に記載の膜モジュールを具備する膜ろ過装置を用い、物理洗浄を定期的に行いながら水処理を行ない透過水を製造する水処理方法。 A water treatment method for producing permeated water by using a membrane filtration apparatus comprising the membrane module according to claim 3 and performing water treatment while periodically performing physical cleaning. 請求項4に記載の水処理方法において、物理洗浄が逆流洗浄である水処理方法。 The water treatment method according to claim 4, wherein the physical washing is backflow washing. 請求項4に記載の水処理方法において、物理洗浄を行う間隔が10分毎以上60分毎以下である水処理方法。 5. The water treatment method according to claim 4, wherein the physical cleaning interval is 10 minutes or more and 60 minutes or less. 請求項5に記載の水処理方法において、使用される分離膜が中空糸膜である水処理方法。 The water treatment method according to claim 5, wherein the separation membrane used is a hollow fiber membrane.
JP2006216910A 2006-08-09 2006-08-09 Membrane module and water-treating method Pending JP2008036574A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006216910A JP2008036574A (en) 2006-08-09 2006-08-09 Membrane module and water-treating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006216910A JP2008036574A (en) 2006-08-09 2006-08-09 Membrane module and water-treating method

Publications (2)

Publication Number Publication Date
JP2008036574A JP2008036574A (en) 2008-02-21
JP2008036574A5 true JP2008036574A5 (en) 2009-11-26

Family

ID=39172193

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006216910A Pending JP2008036574A (en) 2006-08-09 2006-08-09 Membrane module and water-treating method

Country Status (1)

Country Link
JP (1) JP2008036574A (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0278425A (en) * 1987-06-26 1990-03-19 Rhone Poulenc Rech Hydrophilic and dryable semipermeable membrane based on polyvinylidene fluoride
JP3093811B2 (en) * 1991-04-08 2000-10-03 旭化成工業株式会社 Polyvinylidene fluoride resin film and method for producing the same
EP1520874B1 (en) * 2002-06-14 2011-12-28 Toray Industries, Inc. Porous membrane and method of manufacturing the porous membrane

Similar Documents

Publication Publication Date Title
El-Samak et al. Designing flexible and porous fibrous membranes for oil water separation—A review of recent developments
Liu et al. Review on the aerogel-type oil sorbents derived from nanocellulose
Han et al. Thin-film composite (TFC) hollow fiber membrane with double-polyamide active layers for internal concentration polarization and fouling mitigation in osmotic processes
Han et al. Robust and high performance pressure retarded osmosis hollow fiber membranes for osmotic power generation
AU2010206061B2 (en) Highly durable porous PVDF film, method of producing the same and washing method and filtration method using the same
Li et al. Thin-film composite membranes and formation mechanism of thin-film layers on hydrophilic cellulose acetate propionate substrates for forward osmosis processes
KR101657307B1 (en) Fluorinated hollow fiber membrane and method for preparing the same
JP2012115835A (en) Hollow fiber type reverse osmosis membrane
Isık et al. Tailored electrospun fibers from waste polystyrene for high oil adsorption
Yagoub et al. Manipulating the surface wettability of polysaccharide based complex membrane for oil/water separation
JP2009082882A (en) Polyvinylidene fluoride based composite hollow fiber membrane, and its manufacturing method
JP2007181813A (en) Manufacturing method of hollow fiber membrane, and hollow fiber membrane
CN104258742A (en) Preparation method of cheap ultra-filtration membrane for treating oil producing wastewater
JP6368324B2 (en) Porous hollow fiber membrane, method for producing the same, and water purification method
JP4299468B2 (en) Cellulose derivative hollow fiber membrane
JP2008036574A5 (en)
JP2006326497A (en) Semi-permeable membrane for water treatment and its production method
Bakeri et al. Performance of surface‐modified poly (etherimide) hollow‐fiber membranes in a membrane gas Liquid contacting process with response surface methodology
AU715033B2 (en) Polyacrylonitrile-based filtration membrane in a hollow fiber state
JP2004202438A (en) Porous membrane
Zha et al. Polyethersulfone/Cellulose Acetate Butyrate Hybrid Hollow-Fiber Membranes for Organic-Matter Removal From Produced Water
WO2020100763A1 (en) Filtration method in which porous membrane is used
KR101283738B1 (en) Asymmetric ultrafiltration and microfiltration membranes containing chitosan molecules and the method for preparation thereof
KR20160044661A (en) A preparation method of a membrane having improved chlorine resistance and a chlorine resistant membrane prepared by the same
JP2006224051A (en) Porous membrane, porous membrane element, and membrane filter apparatus