JP2006326410A - Membrane for permeating gas selectively - Google Patents
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- 239000012528 membrane Substances 0.000 title claims abstract description 41
- -1 azide compound Chemical class 0.000 claims abstract description 14
- 150000001875 compounds Chemical class 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims description 10
- 229920000642 polymer Polymers 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- 239000007789 gas Substances 0.000 abstract description 49
- 230000035699 permeability Effects 0.000 abstract description 18
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 6
- 239000001301 oxygen Substances 0.000 abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 abstract description 6
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 230000001678 irradiating effect Effects 0.000 abstract 1
- 239000010408 film Substances 0.000 description 9
- 238000005259 measurement Methods 0.000 description 6
- IVRMZWNICZWHMI-UHFFFAOYSA-N azide group Chemical group [N-]=[N+]=[N-] IVRMZWNICZWHMI-UHFFFAOYSA-N 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 4
- 239000002360 explosive Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- OSHFQKSCTZKQMP-UHFFFAOYSA-N 3,3-diazido-2-methyloxetane Chemical compound CC1OCC1(N=[N+]=[N-])N=[N+]=[N-] OSHFQKSCTZKQMP-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 239000005058 Isophorone diisocyanate Substances 0.000 description 2
- PXIPVTKHYLBLMZ-UHFFFAOYSA-N Sodium azide Chemical compound [Na+].[N-]=[N+]=[N-] PXIPVTKHYLBLMZ-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 150000001540 azides Chemical class 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 239000012510 hollow fiber Substances 0.000 description 2
- 150000002466 imines Chemical class 0.000 description 2
- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001308 synthesis method Methods 0.000 description 2
- NLQMSBJFLQPLIJ-UHFFFAOYSA-N (3-methyloxetan-3-yl)methanol Chemical compound OCC1(C)COC1 NLQMSBJFLQPLIJ-UHFFFAOYSA-N 0.000 description 1
- XVLDLRUWOGLKIT-UHFFFAOYSA-N 3-(azidomethyl)-3-methyloxetane Chemical compound [N-]=[N+]=NCC1(C)COC1 XVLDLRUWOGLKIT-UHFFFAOYSA-N 0.000 description 1
- KZMGYPLQYOPHEL-UHFFFAOYSA-N Boron trifluoride etherate Chemical compound FB(F)F.CCOCC KZMGYPLQYOPHEL-UHFFFAOYSA-N 0.000 description 1
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 1
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000000862 absorption spectrum Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- DMLAVOWQYNRWNQ-UHFFFAOYSA-N azobenzene Chemical compound C1=CC=CC=C1N=NC1=CC=CC=C1 DMLAVOWQYNRWNQ-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 125000001033 ether group Chemical group 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- ALIFPGGMJDWMJH-UHFFFAOYSA-N n-phenyldiazenylaniline Chemical compound C=1C=CC=CC=1NN=NC1=CC=CC=C1 ALIFPGGMJDWMJH-UHFFFAOYSA-N 0.000 description 1
- 125000003566 oxetanyl group Chemical group 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002798 polar solvent Substances 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000007142 ring opening reaction Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000007070 tosylation reaction Methods 0.000 description 1
- UDYJJCZCPMQSQG-UHFFFAOYSA-N trimethyl(prop-1-enyl)silane Chemical group CC=C[Si](C)(C)C UDYJJCZCPMQSQG-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
- Polyethers (AREA)
Abstract
Description
本発明は、各種気体を選択的に分離、あるいは、透過させる素材を用いた気体選択透過性膜に関する。 The present invention relates to a gas selective permeable membrane using a material that selectively separates or permeates various gases.
膜による気体分離の機構・方式は、多孔質膜と非多孔質膜に大別されるが、多孔質膜による分離は、孔径が小さく気体がクヌーセン流れのとき可能となる。このとき混合気体の分離選択性は分子量の比の逆数の平方根で表わされ酸素と窒素では、０．９３５４となり、ほぼ１と選択性がほとんど無く、多孔質膜による分離は、困難である。
よって、気体分離は、膜表面での気体分子の溶解、それに続く溶解した気体分子の膜中での拡散、そして最後に、膜からの脱離という溶解拡散機構で説明される非多孔質膜による。
上記技術的背景で、研究開発が活発になされ、酸素冨化、水素分離など実用化研究が進められている。
The mechanism and method of gas separation by a membrane are roughly classified into a porous membrane and a non-porous membrane, but separation by a porous membrane is possible when the pore size is small and the gas is Knudsen flow. At this time, the separation selectivity of the mixed gas is represented by the square root of the reciprocal of the ratio of the molecular weight, and oxygen and nitrogen are 0.9354, almost no selectivity with 1 and separation by the porous membrane is difficult.
Thus, gas separation is due to the non-porous membrane described by the dissolution and diffusion mechanism of dissolution of gas molecules on the membrane surface, followed by diffusion of dissolved gas molecules in the membrane, and finally desorption from the membrane. .
With the above technical background, research and development has been actively carried out, and practical application research such as oxygen enrichment and hydrogen separation is underway.
非多孔質膜における気体の透過量ｑ（ｃｍ3／sec＝立方センチ／秒）は
ｑ＝[S＊D＊（ｐ１−ｐ２）＊A]／ｄ で表わされ、それぞれ
S；溶解度係数 ｃｍ3／ｃｍ3・ｃｍHg
D；拡散係数 ｃｍ2／sec
ｐ１、ｐ２；一次側、および、二次側の当該気体分子の分圧 ｃｍHg
A；膜面積 ｃｍ2
ｄ；膜厚 ｃｍ である。
SとDとは、膜を構成している素材と気体との組み合わせで決まる物性定数であり、
P＝S＊D （ｃｍ3・ｃｍ／ｃｍ2・Sec・ｃｍHg）を透過係数と呼び、
膜素材固有の気体透過特性を評価する重要な物性値になっている。
The gas permeation quantity q (cm 3 / sec = cubic centimeter / second) in the non-porous membrane is represented by q = [S * D * (p1-p2) * A] / d,
S: Solubility coefficient cm 3 / cm 3 · cmHg
D: Diffusion coefficient cm 2 / sec
p1, p2: partial pressure of the gas molecules on the primary side and the secondary side cmHg
A: membrane area cm 2
d: Film thickness cm.
S and D are physical constants determined by the combination of the material and gas that make up the film.
P = S * D (cm 3 · cm / cm 2 · Sec · cmHg) is called the transmission coefficient,
It is an important physical property value for evaluating the gas permeation characteristics unique to the membrane material.
気体を選択的に分離、透過させるためには、
例えば、酸素の透過係数をP（Ｏ2）、窒素の透過係数をP（N2）としたときの透過係数比
α＝P（O2）／P（N2）が大きいことが、必須条件となる。
ところが、非多孔質膜として使用される高分子素材は、α＜１０であり、より高い選択性を有する素材を開発することが、大きな課題であった。
一方、アジドメチル基を有する化合物特性については、本発明者等が、取り扱い安全性の面で検討した結果を公開している（非特許文献１）。
For example, it is essential that the permeability coefficient ratio α = P (O 2 ) / P (N 2 ) is large when the oxygen permeability coefficient is P (O 2 ) and the nitrogen permeability coefficient is P (N 2 ). It becomes.
However, the polymer material used as the non-porous membrane has α <10, and it has been a big problem to develop a material having higher selectivity.
On the other hand, about the characteristic of the compound which has an azidomethyl group, this inventor etc. has published the result examined in terms of handling safety (nonpatent literature 1).
本発明は、気体選択透過性が１０以上の気体選択透過性膜を提供することを目的とする。 An object of the present invention is to provide a gas selective permeable membrane having a gas selective permeability of 10 or more.
本発明者らは、前記課題を解決するため鋭意研究の結果、有機アジド化合物が、極めて高い気体選択透過性を有することを見出し、本発明を完成するに至った。
すなわち、本発明は下記の通りである。
（１） アゾ結合を有する化合物を含有することを特徴とする気体選択透過性膜。
（２） 有機アジド化合物を含有する膜を光照射によって、脱窒素化し、アゾ結合を有する化合物に変換した状態で用いることを特徴とする気体選択透過性膜。
（３） アゾ結合およびエーテル結合を有する重合物を含有することを特徴とする気体選択透過性膜。
（４） 支持基材を用いて膜状に成形されたことを特徴とする（１）〜（３）のいずれかに記載の気体選択透過性膜。
（５） （１）〜（４）のいずれかに記載の気体選択透過性膜が組み込まれたことを特徴とする気体分離装置、気体付与装置、または気体供給装置。
As a result of intensive studies to solve the above problems, the present inventors have found that an organic azide compound has extremely high gas selective permeability, and have completed the present invention.
That is, the present invention is as follows.
(1) A gas selectively permeable membrane comprising a compound having an azo bond.
(2) A gas permeable membrane characterized in that a membrane containing an organic azide compound is denitrogenated by irradiation with light and converted into a compound having an azo bond.
(3) A gas selectively permeable membrane comprising a polymer having an azo bond and an ether bond.
(4) The gas permselective membrane according to any one of (1) to (3), which is formed into a membrane using a supporting base material.
(5) A gas separation device, a gas application device, or a gas supply device, wherein the gas permeable membrane according to any one of (1) to (4) is incorporated.
以下、本発明について、特にその好ましい形態を中心に、説明する。
アジド基を有する化合物としては、具体的に化学式を特定する資料として、A. M. Helmy等が「20th Joint Propulsion Conference (Ohio, 1984)」にて講演した標題「Investigation of New Energetic Ingredient for Minimum Signature Propellants」の紀要に記載されるアジド基含有化合物が知られている。
Hereinafter, the present invention will be described with a focus on preferred embodiments.
As a compound having an azide group, AM Helmy et al. Presented the title `` Investigation of New Energetic Ingredient for Minimum Signature Propellants '', which was given by AM Helmy et al. At `` 20th Joint Propulsion Conference (Ohio, 1984) ''. Azide group-containing compounds described in the bulletin are known.
有機系のアジド化合物は、他成分と混合し、シート化する場合、均一化しやすいので好ましい。特に合成のしやすさ、取り扱い性（安全性）等からアジドメチル（Azidomethyl）基を有する化合物が好ましい。例えば、GAP（Glycidyl Azido Polymer）、AMMO（3-azidomethyl-3 methyloxetane），BAMO（3,3-bis azidomethyl oxetane）等が挙げられる。特に、GAP,ＡＭＭＯは、常温で、液状であり、他成分と混合するには好ましく、かつ、製膜後の可とう性が高く、取り扱いがしやすいため、好ましい。 An organic azide compound is preferable because it is easily homogenized when mixed with other components to form a sheet. In particular, a compound having an azidomethyl group is preferred from the viewpoint of ease of synthesis, handleability (safety), and the like. Examples thereof include GAP (Glycidyl Azido Polymer), AMMO (3-azidomethyl-3 methyloxetane), BAMO (3,3-bis azidomethyl oxetane) and the like. In particular, GAP and AMMO are preferable because they are liquid at room temperature, are preferable for mixing with other components, have high flexibility after film formation, and are easy to handle.
製膜には、支持基材を用いることが好ましい。
支持基材としては、多孔質膜として用いられるものが、好ましく、例えばポリスルホン、ポリエーテルスルホン、ポリアクリロニトリル、酢酸セルロース、ポリオレフィン系などが、利用できる。アルミナ、ジルコニア、チタニアなどの無機素材を利用してもよい。ただ、気体透過係数が、本発明の単独膜よりも、大なる基材であれば、非多孔質の基材も使用できる。例えば、ポリ（トリメチルシリル）プロピレンなどである。
膜の形態は、シート状、テープ状、またはチューブ状（中空繊維状を含む）等、目的に応じて任意に選択できる。
It is preferable to use a supporting substrate for film formation.
As the support substrate, those used as a porous membrane are preferable, and for example, polysulfone, polyethersulfone, polyacrylonitrile, cellulose acetate, polyolefin, and the like can be used. Inorganic materials such as alumina, zirconia, and titania may be used. However, a non-porous substrate can be used as long as the gas permeability coefficient is larger than that of the single membrane of the present invention. For example, poly (trimethylsilyl) propylene.
The form of the membrane can be arbitrarily selected according to the purpose, such as a sheet form, a tape form, or a tube form (including a hollow fiber form).
アジドメチル基を有する化合物特性は、本発明者等が、取り扱い安全性の面で検討した結果を公開している（「工業火薬」第５１巻、第４号（工業火薬協会、１９９０年）第２４０〜２４５ページ）。
これらアジド化合物は、光（電磁波、ここでは、電子線を含む。水銀灯などの紫外線照射器、あるいは、レーザー発信機から生起される。）によって、分解する。
上記文献に、光との反応性を記しているが、具体的には、下式に示すような、機構で、アゾ結合（−N=N−）、あるいは、イミン（−CH＝NH）が生起される。アゾ結合は、赤外線吸収スペクトル（IR）では、１４２９ｃｍ−１付近に吸収が認められ、また、イミンは、１６６６ｃｍ−１ に認められる。
The characteristics of the compound having an azidomethyl group have been disclosed by the present inventors as a result of examination in terms of handling safety (“Industrial Explosives” Vol. 51, No. 4 (Industrial Explosives Association, 1990) No. 240. ~ 245 pages).
These azide compounds are decomposed by light (including electromagnetic waves, here, electron beams; generated from an ultraviolet irradiator such as a mercury lamp or a laser transmitter).
Although the reactivity with light is described in the above-mentioned document, specifically, an azo bond (-N = N-) or imine (-CH = NH) is represented by a mechanism as shown in the following formula. Is born. In the infrared absorption spectrum (IR), absorption of azo bond is observed in the vicinity of 1429 cm −1 , and imine is observed in 1666 cm −1 .
上記、反応が、光照射によって生じるため、用いた有機アジド化合物同士が、結合し、より安定な状態となると考えられる。この状態では、光にさらされても、高温でも、有機アジドの状態に比べ、安定である。主鎖が、ポリエーテル、側鎖同士がアゾ結合で網目構造をとることで、安定化する。膜強度も向上する。 Since the reaction is caused by light irradiation, the organic azide compounds used are considered to be bonded to each other and become more stable. In this state, it is stable compared to the state of organic azide even when exposed to light or at a high temperature. The main chain is a polyether, and the side chains are stabilized by forming a network structure with azo bonds. The film strength is also improved.
これら素材は、気体選択透過性が１０以上であり、気体分離装置、気体付与装置、気体供給装置（例えば、自動車エンジン等への酸素供給）などに有効に用いられる。これら素材をシステム（装置）として機能させるためには、一次側膜面に気体を濃度分極が起こらないような速さで供給し、二次側では、透過した期待をすばやく取り出せるように、膜と膜両側の気体流路を一つのユニットにして、モジュール化してもよい。
これら装置に用いる場合は、比表面積を大にするため、中空繊維状、あるいは、多層膜状にして用いてもよい
These materials have a gas selective permeability of 10 or more, and are effectively used for gas separation devices, gas application devices, gas supply devices (for example, oxygen supply to automobile engines and the like) and the like. In order for these materials to function as a system (device), gas is supplied to the primary membrane surface at a speed that does not cause concentration polarization, and on the secondary side, the membrane and The gas flow paths on both sides of the membrane may be integrated into a single unit.
When used in these devices, it may be used in the form of a hollow fiber or a multilayer film in order to increase the specific surface area.
また、理論的には、窒素が脱離することにより、極めてミクロ的にはポーラス（多孔質）になっていると考えられ、気体透過係数を実測すると有機アジド化合物を含有した状態の初期状態に比べ、光照射後は、気体透過係数は、増加する。このことは、気体の透過量の絶対値を上げることが必要な場合、光の照射量、時間を変えることで制御が可能となる。
この状態の気体透過係数を実測した結果を実施例で示すが、結果から見て、気体の選択透過性を向上させるには、アゾ結合を有する化合物なら、良好な特性を有すると考えられ、有機アジドを光照射によって、脱窒素した化合物でなくても、アゾベンゼン、ジアゾアミノベンゼン、アゾメタンなどの化合物を利用することも可能である。イミン結合を有する化合物も利用できる。
Theoretically, it is considered that the microscopic porous structure is obtained by desorption of nitrogen, and when the gas permeability coefficient is measured, the initial state of the state containing the organic azide compound is obtained. In comparison, the gas permeability coefficient increases after light irradiation. This can be controlled by changing the light irradiation amount and time when it is necessary to increase the absolute value of the gas permeation amount.
The results of actual measurement of the gas permeability coefficient in this state are shown in the Examples. From the results, it is considered that a compound having an azo bond has good characteristics in order to improve the gas selective permeability. It is also possible to use compounds such as azobenzene, diazoaminobenzene, azomethane, etc., even if they are not compounds obtained by denitrifying azide by light irradiation. A compound having an imine bond can also be used.
選択性が発現される理由として、アジド基が有する電子雲が、各種気体と電磁気的作用をし、溶解・拡散を促進、阻害しているものと思われる。
また、さらには、ポリマー中、あるいは、モノマー中に存在するエーテル結合（たとえば、オキセタン環中、および開環重合物）が、関与し、アジド基とエーテル基が両方存在することにより、選択性向上に寄与しているとも推察される。このことにより、有機アジド化合物と他のエーテル結合を有する物質との併用、あるいは、共重合物も同様の選択性を有すると考えられる。
The reason why the selectivity is expressed is that the electron cloud of the azide group has an electromagnetic action with various gases, and promotes and inhibits dissolution / diffusion.
Furthermore, the ether bond (for example, in the oxetane ring and the ring-opening polymer) existing in the polymer or in the monomer is involved, and both the azide group and the ether group are present to improve selectivity. It is assumed that it contributes to Accordingly, it is considered that the combined use or copolymer of the organic azide compound and another substance having an ether bond has the same selectivity.
以下に、本発明の実施例について更に具体的に説明する。
下記実施例で用いたポリマーは，下記合成方法で作成した。
（合成方法、AMMO）
3−メチル−3−ヒドロキシメチルオキセタンをトシル化した後、極性溶媒中で、アジ化ソーダを使用して、アジド化し、AMMOモノマーを得た。このモノマーを三フッ化ホウ素エチルエーテルを重合触媒として１，４ブタンジオールを開始剤としてジクロロメタン溶媒中で重合し，ポリマーを得る事ができた。
本発明の効果を実証するために、以下の実験を実施した。
Hereinafter, examples of the present invention will be described more specifically.
The polymer used in the following examples was prepared by the following synthesis method.
(Synthesis method, AMMO)
After tosylation of 3-methyl-3-hydroxymethyloxetane, azidation was performed using sodium azide in a polar solvent to obtain an AMMO monomer. This monomer was polymerized in a dichloromethane solvent using boron trifluoride ethyl ether as a polymerization catalyst and 1,4 butanediol as an initiator, and a polymer was obtained.
In order to demonstrate the effect of the present invention, the following experiment was conducted.
AMMOポリマー１００ｇに対してＩＰＤＩ（イソホロンジイソシアネート）を８．６ｇ、ＴＰＡ−１００（ヘキサメチレンジイソシアネートのアダクト物（旭化成株式会社製））を３．４ｇ均一混合し、バーコーターを使用し、PETシート上に薄く延ばし、６０℃で加温して硬化させた。得られた薄膜を、低真空法による気体透過測定を実施した。 8.6 g of IPDI (isophorone diisocyanate) and 3.4 g of TPA-100 (adduct of hexamethylene diisocyanate (manufactured by Asahi Kasei Co., Ltd.)) are uniformly mixed with 100 g of AMMO polymer, and a PET coater is used on a PET sheet. The film was spread thinly and heated at 60 ° C. to cure. The obtained thin film was subjected to gas permeation measurement by a low vacuum method.
＜低真空法＞膜の片方の面を低真空（10-1〜10-2 mmHg）に保ち、もう一方の面に大気圧で測定気体を満たすことで、測定気体が低圧側に移動する速度を測定し気体透過係数を導出する測定手法。
測定には、ツクバリカセイキ（株）製K-315-N（商標）を用いた。
測定値は、AMMOの厚みを測定し、PETシートを単独で測定した値を除して、算出した。
その結果、酸素、窒素の気体透過係数の比は、２５℃において、
α＝P(O2)／P（N２）≒５０ となり、極めて高い選択性を有していることが、確認された。
また、二酸化炭素では、P(CO2)＝２．３７×１０−１１という結果であった。
上記サンプルに、紫外線照射（水銀灯）機で、１００ｍJ／平方センチの照射を行い、気体透過性の測定を実施した。
P(CO2)＝４．６４×１０−１１で照射前に比べ、数値が幾分増加した。
またαは、α≒５０となり、高い選択性は維持されていた。
<Low vacuum method> The speed at which the measurement gas moves to the low pressure side by keeping one side of the membrane in a low vacuum (10 -1 to 10 -2 mmHg) and filling the other side with the measurement gas at atmospheric pressure Measurement method to measure gas and derive gas permeability coefficient.
For measurement, K-315-N (trademark) manufactured by Tsukubarika Seiki Co., Ltd. was used.
The measured value was calculated by measuring the thickness of AMMO and dividing the value obtained by measuring the PET sheet alone.
As a result, the ratio of gas permeability coefficients of oxygen and nitrogen is 25 ° C.
α = P (O 2 ) / P (N 2 ) ≈50 and it was confirmed that the film had extremely high selectivity.
For carbon dioxide, the result was P (CO 2 ) = 2.37 × 10 −11 .
The sample was irradiated with 100 mJ / square centimeter with an ultraviolet irradiation (mercury lamp) machine, and gas permeability was measured.
When P (CO 2 ) = 4.64 × 10 −11 , the numerical value increased somewhat compared to before irradiation.
Α was α≈50, and high selectivity was maintained.
ＢＡＭＯポリマーをクロロホルム中に０．１５ｇ／ｍｌ程度の濃度で調整し、ＰＥＴシート上にスピンコーターで塗布した後、溶剤を揮発させ、製膜した。
気体の選択透過性を、実施例１と同様に測定した。
α＝P(O2)／P（N２）（２５℃）≒４０であった。
実施例Ｉと同様に光を照射し、測定を実施した。
α≒３２であった。照射後で比率は低下したが、α＞１０という高い結果であった。
The BAMO polymer was adjusted to a concentration of about 0.15 g / ml in chloroform and coated on a PET sheet with a spin coater, and then the solvent was evaporated to form a film.
The gas selective permeability was measured in the same manner as in Example 1.
α = P (O 2 ) / P (N 2 ) (25 ° C.) ≈40.
In the same manner as in Example I, irradiation was performed and measurement was performed.
α≈32. Although the ratio decreased after irradiation, it was a high result of α> 10.
本発明は、気体分離膜分野で好適に利用できる。
The present invention can be suitably used in the field of gas separation membranes.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006326409A (en) * | 2005-05-24 | 2006-12-07 | Asahi Kasei Chemicals Corp | Material for permeating gas selectively |
| JP2013083965A (en) * | 2011-09-27 | 2013-05-09 | Canon Inc | Optical element and method for manufacturing optical element |
| JP2014508640A (en) * | 2011-02-16 | 2014-04-10 | ダウ コーニング コーポレーション | Method for coating porous substrate |
| CN106732641A (en) * | 2016-11-14 | 2017-05-31 | 江苏省陶瓷研究所有限公司 | A kind of new ceramic-film tube with catalysis and preparation method thereof |
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| US3336268A (en) * | 1963-10-14 | 1967-08-15 | Hercules Inc | Bridged polypropylene |
| JPH0389925A (en) * | 1989-10-25 | 1991-04-15 | Daikin Ind Ltd | Gas separation membrane |
| JP2006326409A (en) * | 2005-05-24 | 2006-12-07 | Asahi Kasei Chemicals Corp | Material for permeating gas selectively |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3336268A (en) * | 1963-10-14 | 1967-08-15 | Hercules Inc | Bridged polypropylene |
| JPH0389925A (en) * | 1989-10-25 | 1991-04-15 | Daikin Ind Ltd | Gas separation membrane |
| JP2006326409A (en) * | 2005-05-24 | 2006-12-07 | Asahi Kasei Chemicals Corp | Material for permeating gas selectively |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006326409A (en) * | 2005-05-24 | 2006-12-07 | Asahi Kasei Chemicals Corp | Material for permeating gas selectively |
| JP2014508640A (en) * | 2011-02-16 | 2014-04-10 | ダウ コーニング コーポレーション | Method for coating porous substrate |
| JP2013083965A (en) * | 2011-09-27 | 2013-05-09 | Canon Inc | Optical element and method for manufacturing optical element |
| CN104985842A (en) * | 2011-09-27 | 2015-10-21 | 佳能株式会社 | Optical element and method for manufacturing the same |
| US9835765B2 (en) | 2011-09-27 | 2017-12-05 | Canon Kabushiki Kaisha | Optical element and method for manufacturing the same |
| CN106732641A (en) * | 2016-11-14 | 2017-05-31 | 江苏省陶瓷研究所有限公司 | A kind of new ceramic-film tube with catalysis and preparation method thereof |
| CN106732641B (en) * | 2016-11-14 | 2019-09-20 | 江苏省陶瓷研究所有限公司 | A kind of novel ceramic-film tube and preparation method thereof with catalysis |
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