JPH11123328A - Adsorbing/desorbing material and its production - Google Patents

Adsorbing/desorbing material and its production

Info

Publication number
JPH11123328A
JPH11123328A JP30650397A JP30650397A JPH11123328A JP H11123328 A JPH11123328 A JP H11123328A JP 30650397 A JP30650397 A JP 30650397A JP 30650397 A JP30650397 A JP 30650397A JP H11123328 A JPH11123328 A JP H11123328A
Authority
JP
Japan
Prior art keywords
adsorbent
resin
solution
porous
poly
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.)
Withdrawn
Application number
JP30650397A
Other languages
Japanese (ja)
Inventor
Yoshiyuki Miyaki
義行 宮木
Kuniyuki Goto
邦之 後藤
Kazuhiko Morio
和彦 森尾
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Adeka Corp
Arkema KK
Original Assignee
Elf Atochem Japan KK
Asahi Denka Kogyo KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Elf Atochem Japan KK, Asahi Denka Kogyo KK filed Critical Elf Atochem Japan KK
Priority to JP30650397A priority Critical patent/JPH11123328A/en
Publication of JPH11123328A publication Critical patent/JPH11123328A/en
Withdrawn legal-status Critical Current

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  • Processes Of Treating Macromolecular Substances (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PROBLEM TO BE SOLVED: To facilitate the production and handling of a product which has a low bulk density, is good in adhesion, water resistance, and thermal stability, and exhibits no deterioration in adsortion/desorption performance in comparison with a powdered adsorbent by dispersing an adsorbent in a poly(ether sulfone) resin. SOLUTION: An adsorbent is preferably in the form of a fine powder in view of dispersability. An adsorbing/desorbing material can be obtained from a solution in which the adsorbent is dispersed uniformly in a poly(ether sulfone) resin solution by a so-called sol-gel method. In a practical operation, for example, after the solution in which the adsorbent is dispersed in the poly(ether sulfone) resin solution being applied on a substrate, it is immersed in a solvent (nonsolvent) which poorly dissolves the poly(ether sulfone) resin and has affinity with a solvent used for dissolving the resin used for dissolving the resin to obtain a coating film in which adsorbent particles are not flocculated in a poly(ether sulfone) resin porous material but are dispersed uniformly as fine particles.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は新規な吸・脱着材料、そ
の製造方法とに関するものである。本発明の吸・脱着材
料は加速された吸着・脱着性能を有し、吸着材料、脱臭
材料、湿度調節材料、分離材料、触媒材料等として使用
することができる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a novel adsorption / desorption material and a method for producing the same. The absorption / desorption material of the present invention has accelerated adsorption / desorption performance, and can be used as an adsorption material, a deodorant material, a humidity control material, a separation material, a catalyst material and the like.

【0002】[0002]

【従来の技術】活性炭をはじめとする嵩密度が高い粉体
の吸着剤は取り扱いが難しいためバインダーを用いてこ
れらの吸着剤を固形化することが行われている。しか
し、バインダーを使用すると吸着剤の細孔が遮断、閉塞
されるため、吸着剤の見かけの表面積が低下し、吸着能
が著しく損なわれてしまう。
2. Description of the Related Art Powdered adsorbents having a high bulk density, such as activated carbon, are difficult to handle, so that these adsorbents are solidified using a binder. However, when a binder is used, the pores of the adsorbent are blocked or closed, so that the apparent surface area of the adsorbent is reduced and the adsorbability is significantly impaired.

【0003】特開平7-41596 には、懸濁重合法で得られ
る多孔質なポリマーゲルを用いて、吸着性能を損なわず
に、活性炭を多孔質ポリマー粒子で被覆した活性炭粒子
を製造する方法が開示されている。しかし、この方法で
調製された活性炭のBET法による表面積は約3分の1
に低下する。しかも、重合反応と同時に活性炭を包摂す
る必要があるため、十分な量の活性炭を添加することが
できず、収率も良くなく、得られた粒子状活性炭からの
粉落ちもみられる。
Japanese Patent Application Laid-Open No. 7-41596 discloses a method for producing activated carbon particles in which activated carbon is coated with porous polymer particles using a porous polymer gel obtained by a suspension polymerization method without impairing the adsorption performance. It has been disclosed. However, the surface area of the activated carbon prepared by this method by the BET method is about one-third.
To decline. In addition, since activated carbon must be included at the same time as the polymerization reaction, a sufficient amount of activated carbon cannot be added, the yield is not good, and powder falls off from the obtained particulate activated carbon.

【0004】特開平02-17989には、活性炭の粒径より大
きい粒径の熱可塑性樹脂粉体を混合して成形する方法が
開示されている。しかし、この方法では多孔性を損なわ
ずに樹脂粉体を成形する必要があるため、成形条件の設
定が難しく、また、この方法で成型された成形物の使用
上の強度は十分とはいえない。
Japanese Patent Application Laid-Open No. 02-17989 discloses a method of molding by mixing a thermoplastic resin powder having a particle size larger than the particle size of activated carbon. However, in this method, it is necessary to mold the resin powder without impairing the porosity, so setting the molding conditions is difficult, and the strength of the molded article molded by this method is not sufficient. .

【0005】特開63-109046 には、活性炭と多孔質ウレ
タンとを組合せた結露防止シートが提案されている。し
かし、この方法で作られたシートが十分な性能を発揮す
るためには、粒径の大きな活性炭を用いる必要がある。
そのため、活性炭の離脱を防止するためにポーラスウレ
タン層を多層にオーバーコートする必要がある。さら
に、ウレタン樹脂の性質上、耐水性、耐熱性に劣る。
[0005] Japanese Patent Application Laid-Open No. 63-109046 proposes a dew condensation preventing sheet in which activated carbon and porous urethane are combined. However, in order for the sheet produced by this method to exhibit sufficient performance, it is necessary to use activated carbon having a large particle size.
Therefore, it is necessary to overcoat the porous urethane layer in multiple layers in order to prevent the detachment of the activated carbon. Furthermore, due to the properties of the urethane resin, the water resistance and heat resistance are poor.

【0006】特開53-28094には、吸着剤として活性炭を
含むポリアクリロニトリル共重合体溶液をゾル・ゲル転
移法によって溶液中の不純物を除去する方法が開示され
ており、ポリスルホンでも実施できる旨の例示がある。
しかし、この組合わせで得られた膜は、吸着剤の孔をポ
リアクリロニトリルなどの樹脂が著しく塞いでしまうた
め、気体の吸着速度、吸着量が減少する。また、耐溶剤
性や耐熱性に劣るため温度スイングなどによる繰り返し
の使用ができない。
Japanese Patent Application Laid-Open No. 53-28094 discloses a method of removing impurities in a polyacrylonitrile copolymer solution containing activated carbon as an adsorbent by a sol-gel transition method. There are examples.
However, in the membrane obtained by this combination, the pores of the adsorbent are significantly blocked by a resin such as polyacrylonitrile, so that the gas adsorption speed and the amount of adsorption decrease. In addition, since it has poor solvent resistance and heat resistance, it cannot be used repeatedly due to a temperature swing or the like.

【0007】[0007]

【発明が解決しようとする課題】本発明の目的は、密着
性、耐水性、耐溶剤性および熱的安定性を兼ね備え、公
知の粉体状吸着剤と比較した場合に吸・脱着性能が低下
しない、嵩密度が低く、製造・取扱いが容易な吸・脱着
材料を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide adhesiveness, water resistance, solvent resistance, and thermal stability, and to decrease the absorption / desorption performance as compared with a known powdery adsorbent. An object of the present invention is to provide an absorbent / desorbable material which has low bulk density and is easy to manufacture and handle.

【0008】本発明者達は、吸着剤と多孔質フィルムを
形成し得る耐熱性、耐薬品性の高分子化合物との複合材
料の性能を幅広く研究する過程で、ポリエーテル系の高
分子と吸着剤とを複合することによって基材密着性と多
孔性とに優れた塗膜が得られということ、しかも、驚く
べきことに、その吸・脱着性能を相当する原料の吸着剤
よりも優れているということを見出し、本発明を完成し
た。
The present inventors have studied a wide range of properties of a composite material of a heat-resistant and chemical-resistant polymer compound capable of forming a porous film with an adsorbent, and have found that a polyether-based polymer is adsorbed with a polyether-based polymer. That the composite with the agent gives a coating film with excellent substrate adhesion and porosity, and surprisingly, its absorption and desorption performance is superior to that of the corresponding raw material adsorbent Thus, the present invention has been completed.

【0009】[0009]

【課題を解決するための手段】本発明が提供する吸・脱
着性材料は、ポリエーテルスルホン系樹脂中に吸着剤が
分散している点に特徴がある。本発明は上記吸・脱着性
材料の製造方法を提供する。本発明方法は、ポリエーテ
ルスルホン系樹脂を溶媒に溶かした溶媒中に吸着剤を分
散させ、得られた溶液をポリエーテルスルホン系樹脂の
非溶媒と接触させる点に特徴がある。本発明のさらに他
の対象は、吸着剤をポリエーテルスルホン系樹脂中に分
散させた複合材料の吸・脱着性材料としての使用にあ
る。
The absorbing / desorbing material provided by the present invention is characterized in that an adsorbent is dispersed in a polyethersulfone resin. The present invention provides a method for producing the above-mentioned absorbent / desorbable material. The method of the present invention is characterized in that an adsorbent is dispersed in a solvent obtained by dissolving a polyethersulfone resin in a solvent, and the obtained solution is brought into contact with a non-solvent of the polyethersulfone resin. Still another object of the present invention is to use a composite material in which an adsorbent is dispersed in a polyethersulfone-based resin as a material for absorbing and desorbing.

【0010】[0010]

【発明の実施の形態】本発明で使用されるポリエーテル
スルホン系樹脂とは、分子内に耐熱性の芳香族スルホン
基と芳香族のエーテル基とを有する樹脂を意味する。こ
のポリエーテルスルホン系樹脂は一般に優れた耐熱性、
機械強度および耐薬品性を示す。好ましいポリエーテル
スルホン系樹脂は1%ジメチルホルムアミドで測定した
還元粘度が0.1 以上かつ1以下のものから選択される。
BEST MODE FOR CARRYING OUT THE INVENTION The polyethersulfone resin used in the present invention means a resin having a heat-resistant aromatic sulfone group and an aromatic ether group in a molecule. This polyether sulfone resin generally has excellent heat resistance,
Shows mechanical strength and chemical resistance. Preferred polyethersulfone resins are selected from those having a reduced viscosity of 0.1 or more and 1 or less measured with 1% dimethylformamide.

【0011】吸着剤の形態は特に問題ではないが、分散
性の観点からは微粉末状のものが好ましく、直径が 100
μm以下であるのが望ましい。吸着剤の種類も特に限定
されないが、活性炭、グラファイト、木炭、ゼオライ
ト、アルミノシリケート、フライポンタイト、酸化マグ
ネシウム、金属フタロシアニン、セピオライト、ベント
ナイト、多孔質シリカ、カオリナイト、珪酸カルシウ
ム、モンモリロナイト、ハロサイト、ヒドロキシアパタ
イト、アロフェン、珪藻土、その他の粘土鉱物、金属酸
化物などを例ですることができる。また、これらの吸着
剤は表面を修飾し、変成し、他の性能を付加し、向上さ
れたものを使用することもできる。
Although the form of the adsorbent is not particularly problematic, it is preferably in the form of a fine powder from the viewpoint of dispersibility,
It is desirable that it is not more than μm. Although the type of the adsorbent is not particularly limited, activated carbon, graphite, charcoal, zeolite, aluminosilicate, fryponite, magnesium oxide, metal phthalocyanine, sepiolite, bentonite, porous silica, kaolinite, calcium silicate, montmorillonite, halosite, Examples include hydroxyapatite, allophane, diatomaceous earth, other clay minerals, metal oxides, and the like. In addition, these adsorbents can be used to modify and modify the surface, add other performances, and improve them.

【0012】ポリエーテルスルホン系樹脂中に分散させ
る吸着剤の量はポリエーテルスルホン系樹脂 100重量部
に対して10〜200 重量部が好ましい。10重量部未満の場
合には吸着性能が不十分であるだけでなく、得られた塗
膜の密着性、平滑性が乏しくなり、200 重量部を越える
と粉落ちが起こり、得られた吸着剤含有高分子多孔体の
機械的強度が低下する。
The amount of the adsorbent dispersed in the polyethersulfone resin is preferably from 10 to 200 parts by weight based on 100 parts by weight of the polyethersulfone resin. If the amount is less than 10 parts by weight, not only the adsorption performance is insufficient, but also the adhesion and smoothness of the obtained coating film become poor. The mechanical strength of the containing polymer porous body decreases.

【0013】本発明の吸・脱着材料は上記の吸着剤をポ
リエーテルスルホン系樹脂溶液に均一に分散させた溶液
から、所謂ゾル−ゲル法によって得ることができる。ポ
リエーテルスルホン系樹脂を溶解させる溶媒は特に限定
されないが、代表的なものとしてはN−メチルピロリド
ン、ホルムアミド、ジメチルホルムアミド、ジメチルア
セトアミド、ジメチルスルホキシド、γ−ブチロラクト
ン、テトラメチルウレア、トリメチルホスフェ−ト等を
挙げることができる。混合溶媒を使用することもでき
る。通常ポリエーテルスルホン系樹脂はこれらの溶媒に
5〜40重量%溶解させる。一方、ポリエーテルスルホン
系樹脂を溶解しない溶媒である非溶媒の例としては水お
よびアルコール類が挙げられる。
The adsorption / desorption material of the present invention can be obtained by a so-called sol-gel method from a solution in which the above adsorbent is uniformly dispersed in a polyethersulfone resin solution. The solvent for dissolving the polyethersulfone resin is not particularly limited, but typical solvents include N-methylpyrrolidone, formamide, dimethylformamide, dimethylacetamide, dimethylsulfoxide, γ-butyrolactone, tetramethylurea, and trimethylphosphate. And the like. Mixed solvents can also be used. Usually, the polyethersulfone resin is dissolved in these solvents in an amount of 5 to 40% by weight. On the other hand, examples of the non-solvent which is a solvent that does not dissolve the polyethersulfone-based resin include water and alcohols.

【0014】塗膜を得る場合には、塗膜の強度、密着性
の観点から非溶媒として水を用いるのが好ましい。ポリ
エーテルスルホン系樹脂を非溶媒に浸漬後、直ちにゾル
・ゲル転移が開始するが、ゲル化を十分に進行させるた
めには10秒以上の浸漬時間をとるのが好ましい。十分な
浸漬時間と乾燥の後に、撥水性の吸着性塗膜が得られ
る。糸を得る場合も、機械的強度の観点から非溶媒とし
て水を用いるのが好ましい。
When a coating film is obtained, it is preferable to use water as the non-solvent from the viewpoint of the strength and adhesion of the coating film. Immediately after the polyethersulfone resin is immersed in the non-solvent, the sol-gel transition starts, but it is preferable to take an immersion time of 10 seconds or more in order to sufficiently promote gelation. After sufficient immersion time and drying, a water-repellent, adsorptive coating is obtained. When a yarn is obtained, it is preferable to use water as a non-solvent from the viewpoint of mechanical strength.

【0015】実際の操作では、例えば吸着剤をポリエー
テルスルホン系樹脂溶液に分散させた溶液を基材上に塗
布した後、ポリエーテルスルホン系樹脂に対して溶解性
が乏しく且つポリエーテルスルホン系樹脂を溶解するの
に用いた溶媒と親和性のある溶媒中 (非溶媒) に浸漬す
ることによって、ポリエーテルスルホン系樹脂多孔体中
に吸着剤粒子が凝集せずに微粒子として均一に分散した
塗膜が得られる。
In an actual operation, for example, a solution in which an adsorbent is dispersed in a polyethersulfone-based resin solution is applied to a substrate, and then the polyethersulfone-based resin is poorly soluble in the polyethersulfone-based resin. By immersing in a solvent (non-solvent) that has an affinity for the solvent used to dissolve the adsorbent, the adsorbent particles are uniformly dispersed as fine particles without agglomeration in the porous polyethersulfone resin. Is obtained.

【0016】基材としては、多孔質基材のみならず非多
孔質基材も用いることができ、いずれの場合も密着性が
強く、膜強度の高い吸着性材料が得られる。多孔質基材
の例としてはステンレス、紙、木材、ガラスまたはプラ
スチックの織布/不織布、多孔質ガラス/セラミックス
などをあげることができる。また、非多孔質基材として
は各種金属箔やシート、プラスチックフィルム・シー
ト、セラミックなどを挙げることができる。
As the substrate, not only a porous substrate but also a non-porous substrate can be used. In any case, an adsorptive material having strong adhesion and high film strength can be obtained. Examples of the porous substrate include stainless steel, paper, wood, glass or plastic woven / nonwoven fabric, porous glass / ceramics, and the like. Further, examples of the non-porous substrate include various metal foils and sheets, plastic films and sheets, and ceramics.

【0017】塗布量は塗膜の厚さが10μm 〜1,000 μm
となるような量が好ましい。塗布量が10μm より少ない
と得られる多孔質膜の空隙率が小さくなり、吸着性能が
低下する。逆に厚さが 1,000μm を越えると、良溶媒、
非溶媒の交換が十分行えず、良好な多孔質膜を得るのが
困難になる。また、ポリエーテルスルホン系樹脂溶液を
基材上に塗布する代わりに、その溶液を紡糸するか、液
滴を非溶媒中に浸漬することによって糸状の吸・脱着材
料にすることもできる。
[0017] The coating amount is 10 μm to 1,000 μm
Is preferably such that If the coating amount is less than 10 μm, the porosity of the obtained porous membrane becomes small, and the adsorption performance is reduced. Conversely, if the thickness exceeds 1,000 μm,
The non-solvent cannot be sufficiently exchanged, and it becomes difficult to obtain a good porous membrane. Instead of applying the polyethersulfone-based resin solution on the base material, the solution may be spun or the droplets may be dipped in a non-solvent to obtain a thread-like absorbing / desorbing material.

【0018】このようにして得られた材料では、吸着剤
がポリエーテルスルホン系樹脂にほとんど覆われること
なく、吸着剤の1次粒子が高分子マトリックスに形成さ
れた細孔中にそのまま独立して存在するという特異な構
造を有している。そのため有機高分子マトリックスがア
セチルセルロース、アクリロニトリル、ポリアミド、ポ
リイミド、ポリエステル等である場合に比べて、吸着速
度に優れた材料を得ることができる。また、ゲル化時に
吸着剤が溶媒とともに脱離することはなく、ほぼ全量の
吸着剤が多孔質高分子マトリックス中に取り込まれるの
で、得られた吸着剤含有多孔体からの吸着剤の粉落ちも
みられない。なお、基材上に形成された塗膜を基材から
剥離して膜を得ることもできる。
In the material thus obtained, the adsorbent is hardly covered with the polyethersulfone-based resin, and the primary particles of the adsorbent are independently and directly contained in the pores formed in the polymer matrix. It has a unique structure that exists. Therefore, a material having an excellent adsorption rate can be obtained as compared with the case where the organic polymer matrix is acetyl cellulose, acrylonitrile, polyamide, polyimide, polyester, or the like. In addition, the adsorbent does not desorb with the solvent at the time of gelation, and almost all of the adsorbent is taken into the porous polymer matrix. I can't. In addition, the coating film formed on the substrate may be peeled from the substrate to obtain a film.

【0019】本発明の吸着性材料には、その性能を損な
わない範囲で、他の高分子化合物や添加剤を加えること
ができる。他の高分子化合物はゾル・ゲル転移法によっ
て多孔質体を形成するものにすることができ、また、多
孔質体のモルフォロジーを制御するための化合物にする
こともできる。添加剤としては各種界面活性剤、分散
剤、顔料、染料、充填剤、水溶性化合物、殺菌剤、その
他の機能性化合物を使用することができる。膜の機械的
強度をさらに向上する目的でガラス、プラスチック、繊
維、金属、金属酸化物のウィスカー等を混合して用いる
こともできる。本発明の吸着性材料はその優れた吸・脱
着性能から、吸着材料、脱臭材料、湿度調節材料、分離
材料、触媒材料として使用することができる。以下、本
発明の実施例を説明するが、本発明が下記実施例に限定
されるものではない。
To the adsorptive material of the present invention, other polymer compounds and additives can be added as long as the performance is not impaired. Other polymer compounds can be used to form a porous body by the sol-gel transition method, and can also be used as compounds for controlling the morphology of the porous body. As the additives, various surfactants, dispersants, pigments, dyes, fillers, water-soluble compounds, bactericides, and other functional compounds can be used. For the purpose of further improving the mechanical strength of the film, glass, plastic, fiber, metal, whisker of metal oxide or the like can be mixed and used. The adsorptive material of the present invention can be used as an adsorbent material, a deodorant material, a humidity control material, a separation material, and a catalyst material because of its excellent absorption / desorption performance. Hereinafter, examples of the present invention will be described, but the present invention is not limited to the following examples.

【0020】[0020]

【実施例】実施例1 15重量部のスミカエクセルPES−4800P(住友化
学社製のポリエーテルスルホン樹脂)を、85重量部のN
−メチルピロリドンに溶解し、この溶液に15重量部のN
K−10(セカ社製のゼオライト粉体) を分散させた。
得られた分散液をガラス板上に流延し、その後水中に浸
漬することによって 200μmの厚さを有する本発明の吸
・脱着材料(基材フィルムを含めて多孔質膜Aという)
を得た。水中には離脱したゼオライト粉末は観測されな
かった。得られた本発明の吸・脱着材料部分の乾燥後の
密度は0.70g/cm3 であった。この乾燥後の多孔質膜A
を室温で90%の湿度を有する雰囲気に5分間静置して重
量増を測定した。重量増はゼオライトの重量に対し15%
であった。すなわち、ゼオライト重量の15%量の水分を
5分間で吸着した。
EXAMPLE 1 15 parts by weight of Sumika Excel PES-4800P (a polyether sulfone resin manufactured by Sumitomo Chemical Co., Ltd.) was mixed with 85 parts by weight of N
-Methylpyrrolidone and 15 parts by weight of N
K-10 (a zeolite powder manufactured by SECA) was dispersed.
The obtained dispersion is cast on a glass plate, and then immersed in water to thereby absorb and desorb the material of the present invention having a thickness of 200 μm (referred to as porous film A including the base film).
I got No detached zeolite powder was observed in the water. The density of the obtained adsorption / desorption material portion of the present invention after drying was 0.70 g / cm 3 . The dried porous membrane A
Was allowed to stand at room temperature in an atmosphere having a humidity of 90% for 5 minutes, and the weight increase was measured. 15% weight gain based on zeolite weight
Met. That is, water of 15% of the weight of the zeolite was adsorbed in 5 minutes.

【0021】比較例1 実施例1と同じ湿度条件下で実施例1と同量のNK−1
0粉体を用いて30分後の重量増を測定した。重量増はゼ
オライトの重量に対して5%であった。これに対して同
じゼオライト粉体を無機系バインダーを用いてビーズ状
に成形した市販品の重量増は30分後で1%であった。こ
のように、本発明の多孔質膜はビーズ状成形品だけでな
く、ゼオライト粉体そのものよりも水分の吸着速度が優
れていた。
Comparative Example 1 The same amount of NK-1 as in Example 1 under the same humidity conditions as in Example 1.
Using 0 powder, the weight increase after 30 minutes was measured. The weight gain was 5% based on the weight of the zeolite. On the other hand, the weight increase of a commercial product obtained by molding the same zeolite powder into beads using an inorganic binder was 1% after 30 minutes. As described above, the porous membrane of the present invention was superior not only to the bead-shaped molded product but also to the zeolite powder itself in the rate of adsorbing moisture.

【0022】比較例2 多孔質高分子前駆体としてポリエーテルスルホン樹脂の
代わりにアクリロニトリル−メタクリル酸共重合体(9
0:10)を使用した他は実施例1と同じ操作でゾル・
ゲル転移を行った。水中に浸漬後、直ちに膜の剥離が観
測された。剥離した塗膜の水蒸気吸収能は10分後に1%
であった。
Comparative Example 2 As a porous polymer precursor, an acrylonitrile-methacrylic acid copolymer (9
0:10), except that sol.
Gel transition was performed. Immediately after immersion in water, peeling of the film was observed. The water absorption capacity of the peeled coating film is 1% after 10 minutes
Met.

【0023】比較例3 実施例1のポリエーテルスルホン樹脂に代えて 200重量
部のポリエチレンアジペートジオール(分子量=2,000)
と、98重量部の4, 4'-ジフェニルメタンジイソシアネー
トと、16重量部のエチレングリコールとから合成した固
形分15%のポリウレタンDMF溶液を用いた。塗布後に
水中に浸浸して得られた多孔質膜の水蒸気吸収能は10分
後で1%であった。このように、本発明の多孔質膜は、
非耐熱性のアクリロニトリル−メタクリル酸共重合体や
ポリウレタンを使用した多孔質膜よりも水分の吸着速度
に優れている。
Comparative Example 3 200 parts by weight of polyethylene adipate diol (molecular weight = 2,000) instead of the polyether sulfone resin of Example 1
And a 15% solids polyurethane DMF solution synthesized from 98 parts by weight of 4,4'-diphenylmethane diisocyanate and 16 parts by weight of ethylene glycol. The water vapor absorption capacity of the porous membrane obtained by immersion in water after coating was 1% after 10 minutes. Thus, the porous membrane of the present invention
It has a higher moisture adsorption rate than a porous film using a non-heat-resistant acrylonitrile-methacrylic acid copolymer or polyurethane.

【0024】実施例2 10重量部のENO(エルフ・アトケム社製の活性炭微粉
末)を実施例1の高分子溶液に分散し、実施例1と同じ
操作で水中に浸漬して活性炭が均一に分散した厚さ 200
μmの本発明の吸・脱着材料を得た(基材フィルムを含
めて多孔質膜Bという)。得られた本発明の吸・脱着材
料部分の乾燥後の密度は0.50g/cm3 であった。この多
孔質膜Bを室温で相対湿度が90%の雰囲気下に静置して
水分吸収能を測定した。30分後に対活性炭重量比で16%
の水分を吸収し、18時間後には対活性炭重量比で37%の
水分を吸収した。また、18時間後のサンプルを室温、相
対湿度50%の雰囲気下に1時間静置したところ、対活性
炭重量比で24%の水分を放出し、水分吸収による重量増
は13%にまで減少していた。
Example 2 10 parts by weight of ENO (fine powder of activated carbon manufactured by Elf Atochem Co.) was dispersed in the polymer solution of Example 1, and immersed in water in the same manner as in Example 1 to make the activated carbon uniform. Dispersed thickness 200
The absorption / desorption material of the present invention having a thickness of μm was obtained (referred to as porous membrane B including the base film). The density of the obtained adsorption / desorption material portion of the present invention after drying was 0.50 g / cm 3 . The porous membrane B was allowed to stand still at room temperature in an atmosphere having a relative humidity of 90%, and the water absorption capacity was measured. After 30 minutes, 16% by weight of activated carbon
, And after 18 hours, 37% of the weight of activated carbon was absorbed. After 18 hours, the sample was allowed to stand for 1 hour in an atmosphere at room temperature and a relative humidity of 50%, and released 24% of water in terms of the weight ratio of activated carbon. The weight increase due to water absorption was reduced to 13%. I was

【0025】比較例4 多孔質高分子前駆体としてポリエーテルスルホン樹脂の
代わりにアクリロニトリル−メタクリル酸共重合体(9
0:10)を使用した他は実施例2と同じ操作でゾル・
ゲル転移を行った。剥離された塗膜の水蒸気吸収能は50
時間後で対活性炭重量比で20%であった。
Comparative Example 4 As a porous polymer precursor, an acrylonitrile-methacrylic acid copolymer (9
0:10), except that sol
Gel transition was performed. The water absorption capacity of the peeled coating film is 50
After an hour, the weight ratio to activated carbon was 20%.

【0026】実施例3 実施例2の活性炭分散高分子溶液をガラス板上に塗布
し、水中に浸漬し、基材から分離して 100μmの本発明
吸・脱着材料(多孔質膜C)を得た。水中に離脱した活
性炭の残存物は観測されなかった。この多孔質膜Cを室
温で乾燥後、室温で飽和ベンゼン蒸気雰囲気中に10分間
静置した。対含有活性炭重量で46%のベンゼンを吸収し
ていた。その後、通常室内に放置したところ10分後には
吸収した90%のベンゼンが脱着されていた。また、この
室温乾燥した多孔質膜Cを 180℃に 100時間静置したの
ち、室温下で飽和ベンゼン蒸気雰囲気中に10分間静置し
た。同様に対含有活性炭重量で46%のベンゼンを吸収し
た。その後、通常室内に放置したところ10分後には吸収
した90%のベンゼンが脱着されていた。このように本発
明の多孔質膜は熱安定性も優れている。さらに、室温乾
燥した多孔質膜Cを〔表1〕に示す各種薬品に各温度で
24時間浸漬し、その外観の変化を目視観察した。その結
果を〔表1〕に示す。このように本発明の多孔質膜は耐
溶剤性にも優れていた。
Example 3 The activated carbon-dispersed polymer solution of Example 2 was applied on a glass plate, immersed in water, and separated from the substrate to obtain a 100 μm absorbing / desorbing material of the present invention (porous membrane C). Was. No activated carbon residue left in the water was observed. After drying the porous film C at room temperature, it was allowed to stand at room temperature in a saturated benzene vapor atmosphere for 10 minutes. 46% of benzene was absorbed by activated carbon weight. After that, when it was usually left in a room, 90% of the absorbed benzene had been desorbed after 10 minutes. The porous film C dried at room temperature was allowed to stand at 180 ° C. for 100 hours, and then allowed to stand at room temperature in a saturated benzene vapor atmosphere for 10 minutes. Similarly, 46% of benzene was absorbed by the weight of activated carbon contained. After that, when it was usually left in a room, 90% of the absorbed benzene had been desorbed after 10 minutes. Thus, the porous membrane of the present invention has excellent thermal stability. Further, the porous membrane C dried at room temperature was added to various chemicals shown in [Table 1] at each temperature.
It was immersed for 24 hours and its appearance was visually observed. The results are shown in [Table 1]. Thus, the porous film of the present invention was excellent also in solvent resistance.

【0027】[0027]

【表1】 [Table 1]

【0028】比較例5 実施例4で使用した微粉末状活性炭を、実施例4と同じ
ベンゼン蒸気に10分間吸収させた。対活性炭重量で35%
のベンゼンを吸収していた。その後の室内放置では、10
分後の脱着量は20%であった。その後、通常室内に放置
したところ、10分後には吸収したベンゼンの20%が脱着
されていた。このように、本発明の多孔質膜は活性炭粉
体そのものよりもベンゼンの吸着速度・脱着速度が優れ
ている。
Comparative Example 5 The fine powdered activated carbon used in Example 4 was absorbed in the same benzene vapor as in Example 4 for 10 minutes. 35% by activated carbon weight
Had absorbed benzene. After that, 10
The desorption amount after one minute was 20%. After that, when it was usually left in a room, 10 minutes later, 20% of the absorbed benzene had been desorbed. Thus, the porous membrane of the present invention is superior in the benzene adsorption and desorption rates to the activated carbon powder itself.

【0029】実施例4 15重量部のスミカエクセルPES−5200P(住友化
学製ポリエーテルスルホン樹脂)を、85重量部のジメチ
ルアセトアミドに溶解した。この溶液に15重量部のライ
オナイトSF(ライオン社製の珪酸塩鉱物系吸着剤)を
分散させ、硝子繊維上に流延し、その後、水中に浸漬す
ることによって硝子繊維に密着性した厚さが 500μmの
本発明吸・脱着材料(基材を含め多孔質膜Dという)を
得た。水中には離脱した珪酸塩鉱物は観測されなかっ
た。この塗膜のサンプル50cm2を 250 ppmのアンモニア
を収容した1.8 リットルの容器に入れ、検知管(北川式
SD型)でアンモニア濃度を測定した。1.5 時間後にアン
モニア濃度は10ppm 以下になっていた。この実験で本発
明の吸・脱着材料はアンモニアを吸着することが示され
た。
Example 4 15 parts by weight of Sumika Excel PES-5200P (a polyether sulfone resin manufactured by Sumitomo Chemical Co., Ltd.) was dissolved in 85 parts by weight of dimethylacetamide. 15 parts by weight of Lionion SF (a silicate mineral-based adsorbent manufactured by Lion Corporation) is dispersed in this solution, cast on glass fibers, and then immersed in water to obtain a thickness that is adhered to the glass fibers. Of the present invention (hereinafter referred to as porous film D including the substrate) having a particle size of 500 μm. No separated silicate mineral was observed in the water. A 50 cm 2 sample of this coating was placed in a 1.8 liter container containing 250 ppm of ammonia and a detector tube (Kitakawa
(SD type). After 1.5 hours, the ammonia concentration had dropped below 10 ppm. This experiment showed that the adsorption / desorption material of the present invention adsorbs ammonia.

【0030】比較例6 実施例4で使用したライオナイトSFの同量を 1.8リッ
トルの容器に入れ、実施例4と同じ操作でアンモニアの
減少速度を測定した。10ppm 以下に達するに4時間を要
した。
Comparative Example 6 The same amount of Lionion SF used in Example 4 was placed in a 1.8-liter container, and the rate of ammonia reduction was measured in the same manner as in Example 4. It took 4 hours to reach below 10 ppm.

【0031】[0031]

【発明の効果】以上の通り、本発明の吸・脱着材料は、
嵩密度が低く、密着性、耐水性、耐溶剤性、熱的安定性
に優れ、吸・脱着性能が粉体状の吸着剤に比較して低下
せず、製造・取り扱いも容易である。
As described above, the adsorbing / desorbing material of the present invention comprises:
It has low bulk density, excellent adhesion, water resistance, solvent resistance, and thermal stability, does not decrease in absorption / desorption performance as compared with powdered adsorbents, and is easy to manufacture and handle.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 後藤 邦之 東京都千代田区紀尾井町3番23号 エル フ・アトケム・ジャパン株式会社内 (72)発明者 森尾 和彦 東京都荒川区東尾久7丁目2番35 旭電化 工業株式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Kuniyuki Goto 3-23 Kioicho, Chiyoda-ku, Tokyo Elf Atochem Japan K.K. Asahi Denka Kogyo Co., Ltd.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 ポリエーテルスルホン系樹脂中に吸着剤
が分散していることを特徴とする多孔質吸・脱着性材
料。
1. A porous adsorbent / desorbable material comprising an adsorbent dispersed in a polyethersulfone resin.
【請求項2】 吸着剤が活性炭、グラファイト、木炭、
ゼオライト、アルミノシリケート、多孔質シリカ、金属
酸化物、粘度鉱物からなる群の中から選択される1 種ま
たは2 種以上である請求項1に記載の吸・脱着性材料。
2. The method according to claim 1, wherein the adsorbent is activated carbon, graphite, charcoal,
2. The absorbent / desorbable material according to claim 1, which is one or more selected from the group consisting of zeolite, aluminosilicate, porous silica, metal oxide, and viscous mineral.
【請求項3】 吸・脱着性材料が気体の吸・脱着用材料
である請求項1または2に記載の吸・脱着性材料。
3. The absorbent / desorbable material according to claim 1, wherein the absorbent / desorbable material is a gas absorbent / desorbable material.
【請求項4】 ポリエーテルスルホン系樹脂を溶媒に溶
かした溶媒中に吸着剤を分散させ、得られた溶液をポリ
エーテルスルホン系樹脂の非溶媒と接触させることを特
徴とする、ポリエーテルスルホン系樹脂中に吸着剤が分
散している多孔質吸・脱着性材料の製造方法。
4. A polyethersulfone-based resin, comprising: dispersing an adsorbent in a solvent in which a polyethersulfone-based resin is dissolved; and contacting the resulting solution with a non-solvent of the polyethersulfone-based resin. A method for producing a porous absorbent / desorbable material in which an adsorbent is dispersed in a resin.
【請求項5】 ポリエーテルスルホン系樹脂中に吸着剤
が分散した複合材料の多孔質吸・脱着性材料としての使
用。
5. Use of a composite material in which an adsorbent is dispersed in a polyethersulfone-based resin as a porous absorbent / desorbable material.
JP30650397A 1997-10-21 1997-10-21 Adsorbing/desorbing material and its production Withdrawn JPH11123328A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JPH11123328A true JPH11123328A (en) 1999-05-11

Family

ID=17957817

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
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Publication number Priority date Publication date Assignee Title
WO2014174756A1 (en) * 2013-04-23 2014-10-30 トヨタ自動車株式会社 Oil deterioration suppressor
JPWO2013187505A1 (en) * 2012-06-14 2016-02-08 株式会社カサイ Radioactive cesium-adsorbing fiber, method for producing the same, and apparatus for detecting the concentration of radioactive cesium in water using the radioactive cesium-adsorbing fiber
JP2020185501A (en) * 2019-05-09 2020-11-19 株式会社カサイ Adsorbent for water purification, manufacturing method of adsorbent for water purification, radioactive substance concentration detector, and land-based aquaculture system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2013187505A1 (en) * 2012-06-14 2016-02-08 株式会社カサイ Radioactive cesium-adsorbing fiber, method for producing the same, and apparatus for detecting the concentration of radioactive cesium in water using the radioactive cesium-adsorbing fiber
WO2014174756A1 (en) * 2013-04-23 2014-10-30 トヨタ自動車株式会社 Oil deterioration suppressor
JP5937752B2 (en) * 2013-04-23 2016-06-22 トヨタ自動車株式会社 Oil deterioration suppressor
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