JP2018118211A - Liquid purifying method, and adsorbent - Google Patents

Liquid purifying method, and adsorbent Download PDF

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JP2018118211A
JP2018118211A JP2017011848A JP2017011848A JP2018118211A JP 2018118211 A JP2018118211 A JP 2018118211A JP 2017011848 A JP2017011848 A JP 2017011848A JP 2017011848 A JP2017011848 A JP 2017011848A JP 2018118211 A JP2018118211 A JP 2018118211A
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liquid
adsorbent
zif
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dioxane
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大輝 今野
Daiki Konno
大輝 今野
奉広 鍵本
Tomohiro Kagimoto
奉広 鍵本
英雄 楳田
Hideo Umeda
英雄 楳田
隆夫 増田
Takao Masuda
隆夫 増田
佑太 中坂
Yuta Nakasaka
佑太 中坂
睦仁 斎藤
Mutsuhito Saito
睦仁 斎藤
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Hokkaido University NUC
Sumitomo Bakelite Co Ltd
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Sumitomo Bakelite Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a liquid purifying method that selectively adsorbs a specific material in liquid to remove it from the liquid.SOLUTION: A liquid purifying method includes the step of bringing a liquid containing a target material into contact with an adsorbent, to make the adsorbent selectively adsorb the target material contained in the liquid, so that it is removed from the liquid. The adsorbent has a metal organic structure of a zeolite imidazolate skeleton comprising zinc or cobalt ions and 2-methyl imidazolate ligands.SELECTED DRAWING: None

Description

本発明は、液体の清浄化方法、および吸着剤に関する。より詳細には、本発明は、液体中の特定物質を吸着除去して液体を清浄化する方法、およびこの方法に用いる吸着剤に関する。   The present invention relates to a liquid cleaning method and an adsorbent. More specifically, the present invention relates to a method for cleaning a liquid by adsorbing and removing a specific substance in the liquid, and an adsorbent used in the method.

従来より、中心金属とこれに配位する多座有機配位子からなる金属錯体が集積し、多孔性の三次元構造体となった金属有機構造体は多数知られている。こうした金属有機構造体は、ゼオライトや活性炭といった他の多孔性材料に比べ、均一な細孔を形成することができることから、水素、二酸化炭素、一酸化炭素、酸素、窒素、炭化水素等の吸着材料や吸蔵材料としての利用が期待され、その構造や合成法に関する研究が進められている(たとえば、特許文献1)   Conventionally, a large number of metal organic structures in which a metal complex composed of a central metal and a multidentate organic ligand coordinated thereto are accumulated to form a porous three-dimensional structure have been known. Since these metal organic structures can form uniform pores compared to other porous materials such as zeolite and activated carbon, adsorption materials such as hydrogen, carbon dioxide, carbon monoxide, oxygen, nitrogen, hydrocarbons, etc. The use as an occlusion material is expected, and research on its structure and synthesis method is underway (for example, Patent Document 1).

このような有機金属構造体を吸着剤として用いる技術は、たとえば、特許文献2に記載されている。特許文献2では、ゼオライト様イミダゾレート構造体ZIF−8の特定のガスに対する吸着能に注目し、これをガスセンサーデバイス等に利用する技術が提案されている。   A technique using such an organometallic structure as an adsorbent is described in Patent Document 2, for example. Patent Document 2 proposes a technique of paying attention to the adsorption ability of a zeolite-like imidazolate structure ZIF-8 to a specific gas and utilizing this in a gas sensor device or the like.

特開2014−28792号公報JP 2014-28792 A 特開2014−156434号公報JP 2014-156434 A

特許文献1および2に開示される技術は、ガスである被処理物中の特定の物質を、金属有機構造体により処理するものである。   The techniques disclosed in Patent Documents 1 and 2 treat a specific substance in an object to be processed, which is a gas, with a metal organic structure.

本発明者らは、液体中の特定の物質を選択的に吸着する吸着剤として、金属有機構造体ZIF−8およびZIF−67の新たな用途を見出し、本発明の完成に至った。   The present inventors have found a new use of the metal organic structures ZIF-8 and ZIF-67 as adsorbents that selectively adsorb specific substances in a liquid, and have completed the present invention.

本発明によれば、対象物質を含む液体と、吸着剤とを接触させて、前記液体に含まれる前記対象物質を選択的に前記吸着剤に吸着させて、前記液体から除去する工程を含む、液体の清浄化方法であって、
前記吸着剤が、亜鉛イオンまたはコバルトイオンと、2−メチルイミダゾレート配位子とからなるゼオライト型イミダゾレート骨格である金属有機構造体を含む、液体の清浄化方法が提供される。
According to the present invention, the method includes a step of bringing a liquid containing a target substance into contact with an adsorbent, selectively adsorbing the target substance contained in the liquid to the adsorbent, and removing the liquid from the liquid. A liquid cleaning method comprising:
There is provided a liquid cleaning method in which the adsorbent includes a metal organic structure that is a zeolite type imidazolate skeleton composed of zinc ions or cobalt ions and a 2-methylimidazolate ligand.

また本発明によれば、金属有機構造体を含む吸着剤であって、
前記金属有機構造体が、亜鉛イオンまたはコバルトイオンと、2−メチルイミダゾレート配位子とからなるゼオライト型イミダゾレート骨格であり、
前記吸着剤が、液体中の対象物質を選択的に吸着する、吸着剤が提供される。
Moreover, according to the present invention, an adsorbent comprising a metal organic structure,
The metal organic structure is a zeolitic imidazolate skeleton composed of zinc ions or cobalt ions and a 2-methylimidazolate ligand;
An adsorbent is provided in which the adsorbent selectively adsorbs a target substance in a liquid.

本発明によれば、排水等の被処理液に含まれる特定の物質を、選択的に、かつ簡単に効率よく、安価に吸着除去できる吸着剤、およびこのような吸着剤を用いて特定物質を除去する液体の清浄化方法が提供される。   ADVANTAGE OF THE INVENTION According to this invention, the specific substance contained in to-be-processed liquids, such as a waste_water | drain, can selectively, simply, efficiently and cheaply adsorb and remove the specific substance using such an adsorbent. A method for cleaning the liquid to be removed is provided.

実施例A1〜A4における、処理前の水溶液の1,4−ジオキサン濃度に対する、ZIF−8で処理後の水溶液の1,4−ジオキサン濃度の関係を示す検量線である。In Example A1-A4, it is a calibration curve which shows the relationship of the 1, 4- dioxane density | concentration of the aqueous solution after processing with ZIF-8 with respect to the 1, 4- dioxane density | concentration of the aqueous solution before a process. 実施例B1〜B4における処理前の有機溶液の1,4−ジオキサン濃度に対する、ZIF−8で処理後の有機溶液の1,4−ジオキサン濃度の関係を示す検量線である。It is a calibration curve which shows the relationship of the 1, 4- dioxane density | concentration of the organic solution after a process with ZIF-8 with respect to the 1, 4- dioxane density | concentration of the organic solution before the process in Example B1-B4. 実施例Cにおける、1,4−ジオキサン、テトラヒドロピラン、およびシクロヘキサンに対する、ZIF−8の、25℃における吸着等温線である。FIG. 5 is an adsorption isotherm at 25 ° C. of ZIF-8 for 1,4-dioxane, tetrahydropyran, and cyclohexane in Example C. FIG. 実施例Eにおける、ベンゼン、トルエン、メチルシクロヘキサン、およびメシチレン(1,3,5−トリメチルベンゼン)に対する、ZIF−8の、25℃における吸着等温線である。2 is an adsorption isotherm at 25 ° C. of ZIF-8 for benzene, toluene, methylcyclohexane and mesitylene (1,3,5-trimethylbenzene) in Example E. 1,4−ジオキサンおよび水に対する、ZIF−8の、25℃における吸着等温線である。2 is an adsorption isotherm of ZIF-8 at 25 ° C. for 1,4-dioxane and water. 1,4−ジオキサンおよび水に対する、活性炭の、25℃における吸着等温線である。2 is an adsorption isotherm at 25 ° C. of activated carbon for 1,4-dioxane and water. 1,4−ジオキサンおよび水に対する、ゼオライトの、25℃における吸着等温線である。2 is an adsorption isotherm at 25 ° C. of zeolite for 1,4-dioxane and water.

以下、本発明の実施の形態について説明する。   Embodiments of the present invention will be described below.

本実施形態の液体の清浄化方法は、対象物質を含む液体と、吸着剤とを接触させて、液体に含まれる対象物質を選択的に吸着剤に吸着させて、前記液体から除去する工程を含む。   The liquid cleaning method of the present embodiment includes a step of bringing a liquid containing a target substance into contact with an adsorbent, selectively adsorbing the target substance contained in the liquid onto the adsorbent, and removing the target substance from the liquid. Including.

本実施形態の方法において、吸着剤は、金属有機構造体であり、この金属有機構造体は、亜鉛イオンと2−メチルイミダゾレート配位子とからなるゼオライト型イミダゾレート骨格(本明細書において、「ZIF−8」と称する)、または、コバルトイオンと2−メチルイミダゾレート配位子とからなるゼオライト型イミダゾレート骨格(本明細書において、「ZIF−67」と称する)である。吸着剤として、ZIF−8またはZIF−67を用いることにより、特定の物質を選択的に効率よく吸着することができる。   In the method of the present embodiment, the adsorbent is a metal organic structure, and the metal organic structure is a zeolite type imidazolate skeleton (in the present specification, composed of a zinc ion and a 2-methylimidazolate ligand). Or a zeolite type imidazolate skeleton (referred to herein as “ZIF-67”) composed of a cobalt ion and a 2-methylimidazolate ligand. By using ZIF-8 or ZIF-67 as the adsorbent, a specific substance can be selectively and efficiently adsorbed.

本発明者らは、ZIF−8およびZIF−67が、特定の有機化合物を吸着するが、水分子をほとんど吸着しないことを見出した。本発明者らは、ZIF−8およびZIF−67が、含酸素有機化合物または芳香族化合物、特に、含酸素六員環化合物またはフェノール性水酸基を有する芳香族化合物、たとえば、1,4−ジオキサン、テトラヒドロピラン、フェノール、ベンゼンおよびトルエンを選択的に吸着することを見出した。   The inventors have found that ZIF-8 and ZIF-67 adsorb specific organic compounds but hardly adsorb water molecules. The inventors have determined that ZIF-8 and ZIF-67 are oxygenated organic compounds or aromatic compounds, particularly oxygenated six-membered ring compounds or aromatic compounds having a phenolic hydroxyl group, such as 1,4-dioxane, It was found to selectively adsorb tetrahydropyran, phenol, benzene and toluene.

図5、図6および図7は、ZIF−8、活性炭およびゼオライトの、1,4−ジオキサンおよび水分子に対する、25℃における吸着等温線である。活性炭は、1,4−ジオキサンと水分子の双方を吸着し(図6)、ゼオライトはこれらのいずれも吸着しない(図7)のに対し、ZIF−8は、1,4−ジオキサンを吸着して、水分子を吸着しない(図5)。そのため、ZIF−8は、たとえば、排水のような水溶液を清浄化処理するための吸着剤として使用できる。また、本発明者らは、ZIF−8は、それが有する細孔径を上回る分子径を有する分子をほとんど吸着しないことを見出した。これにより、本実施形態の方法によれば、例えば、メシチレンのような、分子径がZIF−8の細孔より大きい有機溶媒を含む有機廃液中に存在する特定の有害物質を効率的に吸着除去することができる。   5, 6 and 7 are adsorption isotherms at 25 ° C. for 1,4-dioxane and water molecules of ZIF-8, activated carbon and zeolite. Activated carbon adsorbs both 1,4-dioxane and water molecules (FIG. 6), while zeolite adsorbs none of these (FIG. 7), whereas ZIF-8 adsorbs 1,4-dioxane. Thus, water molecules are not adsorbed (FIG. 5). Therefore, ZIF-8 can be used as an adsorbent for purifying an aqueous solution such as waste water. The present inventors have also found that ZIF-8 hardly adsorbs molecules having a molecular diameter larger than the pore diameter of the ZIF-8. As a result, according to the method of the present embodiment, for example, specific harmful substances existing in an organic waste liquid containing an organic solvent having a molecular diameter larger than the pores of ZIF-8, such as mesitylene, are efficiently adsorbed and removed. can do.

またZIF−67は、ZIF−8と同様の構造を有することから、これと同様の特異的吸着性を有する。   Moreover, since ZIF-67 has the same structure as ZIF-8, it has the same specific adsorptivity as this.

本実施形態において、吸着剤として用いるZIF−8およびZIF−67は、公知の方法により調製されるか、または工業的に入手可能である。   In the present embodiment, ZIF-8 and ZIF-67 used as adsorbents are prepared by known methods or are commercially available.

本実施形態の吸着剤の形態は、例えば、粉状、粒状、顆粒状、ペレット、繊維状、膜、フィルム等であり得る。吸着剤は、必要に応じて、さらなる成分、例えば、樹脂、無機粒子、別の多孔性物質を含んでもよい。   The form of the adsorbent of the present embodiment can be, for example, powder, granule, granule, pellet, fiber, membrane, film or the like. The adsorbent may contain additional components, such as resins, inorganic particles, and other porous materials, if desired.

本実施形態の吸着剤は、公知の任意の方法で使用することが可能であり、そのまま被処理物中に浸漬してもよいし、粒状物やペレットなどをカラムに充填したり、膜状物をフィルターカートリッジに装着する方法で通液使用できる。   The adsorbent of the present embodiment can be used by any known method, and may be immersed in an object to be processed as it is, or it may be filled with granular materials or pellets in a column, or a film-like material. The liquid can be used by attaching to the filter cartridge.

一実施形態において、浄化され得る液体は、水溶液または有機溶液であり、例えば、排水、有機廃液等が挙げられる。   In one embodiment, the liquid that can be purified is an aqueous solution or an organic solution, such as waste water, organic waste liquid, and the like.

以上、本発明の実施形態について述べたが、これらは本発明の例示であり、上記以外の様々な構成を採用することができる。   As mentioned above, although embodiment of this invention was described, these are illustrations of this invention and can employ | adopt various structures other than the above.

以下、実施例を参照して本発明を詳細に説明するが、本発明はこれらの例示に限定されるものではない。   EXAMPLES Hereinafter, although this invention is demonstrated in detail with reference to an Example, this invention is not limited to these illustrations.

(実施例A1〜A4)
実施例A1〜A4において、以下の表に示す量の1,4−ジオキサンが溶解した水溶液4.0mlに、0.10gのZIF−8を混合し、60℃で40時間撹拌した。その後遠心分離により、水溶液を回収し、ガスクロマトグラフィーを用いて水溶液の1,4−ジオキサン量を測定した。また、実施例A1〜A4の結果より、処理前濃度に対する処理後平衡濃度の検量線を作成した(図1)。結果を、以下の表1に併せて示す。
(Examples A1 to A4)
In Examples A1 to A4, 0.10 g of ZIF-8 was mixed with 4.0 ml of an aqueous solution in which 1,4-dioxane of the amount shown in the following table was dissolved, and the mixture was stirred at 60 ° C. for 40 hours. Thereafter, the aqueous solution was recovered by centrifugation, and the amount of 1,4-dioxane in the aqueous solution was measured using gas chromatography. Moreover, the calibration curve of the post-treatment equilibrium concentration with respect to the pre-treatment concentration was prepared from the results of Examples A1 to A4 (FIG. 1). The results are also shown in Table 1 below.

(比較例A1)
ZIF−8を、0.10gの活性炭に替えたこと以外は、実施例A1〜A4と同様の工程を行った。処理後の水溶液中の1,4−ジオキサン濃度を以下の表1に示す。
(Comparative Example A1)
The same steps as in Examples A1 to A4 were performed except that ZIF-8 was replaced with 0.10 g of activated carbon. The 1,4-dioxane concentration in the aqueous solution after treatment is shown in Table 1 below.

(比較例A2)
ZIF−8を、0.10gのゼオライトに替えたこと以外は、実施例A1〜A4と同様の工程を行った。処理後の水溶液中の1,4−ジオキサン濃度を以下の表1に示す。
(Comparative Example A2)
The same steps as in Examples A1 to A4 were performed except that ZIF-8 was changed to 0.10 g of zeolite. The 1,4-dioxane concentration in the aqueous solution after treatment is shown in Table 1 below.

Figure 2018118211
Figure 2018118211

(実施例B1〜B4)
実施例B1〜B4において、以下の表に示す量の1,4−ジオキサンが溶解したメシチレン溶液4.0mlに、0.1gのZIF−8を混合し、40℃で6時間撹拌した。その後遠心分離により、有機層を回収し、ガスクロマトグラフィーを用いて有機層の1,4−ジオキサン量を測定した。また、実施例B1〜B4の結果より、処理前濃度に対する処理後平衡濃度の検量線を作成した(図2)。結果を、以下の表2に併せて示す。
(Examples B1 to B4)
In Examples B1 to B4, 0.1 g of ZIF-8 was mixed with 4.0 ml of a mesitylene solution in which 1,4-dioxane in an amount shown in the following table was dissolved, and the mixture was stirred at 40 ° C. for 6 hours. Thereafter, the organic layer was recovered by centrifugation, and the amount of 1,4-dioxane in the organic layer was measured using gas chromatography. Moreover, the calibration curve of the post-treatment equilibrium concentration with respect to the pre-treatment concentration was created from the results of Examples B1 to B4 (FIG. 2). The results are also shown in Table 2 below.

(比較例B1)
ZIF−8を、0.1gの活性炭に替えたこと以外は、実施例B1〜B4と同様の工程を行った。処理後の水溶液中の1,4−ジオキサン濃度を以下の表2に示す。
(Comparative Example B1)
The same steps as in Examples B1 to B4 were performed except that ZIF-8 was replaced with 0.1 g of activated carbon. The concentration of 1,4-dioxane in the aqueous solution after treatment is shown in Table 2 below.

(比較例B2)
ZIF−8を、0.1gのゼオライトに替えたこと以外は、実施例B1〜B4と同様の工程を行った。処理後の水溶液中の1,4−ジオキサン濃度を以下の表2に示す。
(Comparative Example B2)
The same steps as in Examples B1 to B4 were performed except that ZIF-8 was replaced with 0.1 g of zeolite. The concentration of 1,4-dioxane in the aqueous solution after treatment is shown in Table 2 below.

Figure 2018118211
Figure 2018118211

(実施例C)
1,4−ジオキサン、テトラヒドロピラン、およびシクロヘキサンに対して、吸着剤としてZIF−8を用い、25℃における吸着等温線を作成した。結果を図3に示す。図3に示す結果から、ZIF−8は、1,4−ジオキサン、およびテトラヒドロピランに対して特異的な吸着特性を示すことが分かった。
(Example C)
For 1,4-dioxane, tetrahydropyran, and cyclohexane, an adsorption isotherm at 25 ° C. was prepared using ZIF-8 as the adsorbent. The results are shown in FIG. From the results shown in FIG. 3, it was found that ZIF-8 exhibits specific adsorption characteristics for 1,4-dioxane and tetrahydropyran.

(実施例E)
ベンゼン、トルエン、メチルシクロヘキサン、および1,3,5−トリメチルベンゼンに対して、吸着剤としてZIF−8を用い、25℃における吸着等温線を作成した。結果を図4に示す。図4に示す結果から、ZIF−8は、ベンゼン、およびトルエンに対して特異的な吸着特性を示すことが分かった。
(Example E)
For benzene, toluene, methylcyclohexane, and 1,3,5-trimethylbenzene, an adsorption isotherm at 25 ° C. was prepared using ZIF-8 as the adsorbent. The results are shown in FIG. From the results shown in FIG. 4, it was found that ZIF-8 exhibits specific adsorption characteristics for benzene and toluene.

(実施例D1)
濃度19.0g/Lの1,4−ジオキサン水溶液4.0mlに、0.10gのZIF−67を混合し、60℃で40時間撹拌した。その後遠心分離により、水溶液を回収し、ガスクロマトグラフィーを用いて水溶液の1,4−ジオキサン量を測定した。結果を表3に示す。

Figure 2018118211
(Example D1)
0.10 g of ZIF-67 was mixed with 4.0 ml of a 1,4-dioxane aqueous solution having a concentration of 19.0 g / L, and the mixture was stirred at 60 ° C. for 40 hours. Thereafter, the aqueous solution was recovered by centrifugation, and the amount of 1,4-dioxane in the aqueous solution was measured using gas chromatography. The results are shown in Table 3.
Figure 2018118211

上記実施例から分かるように、ZIF−8およびZIF−67は、水溶液またはメシチレン溶液中の特定の有機化合物を特異的に吸着した。   As can be seen from the above examples, ZIF-8 and ZIF-67 specifically adsorbed specific organic compounds in aqueous solution or mesitylene solution.

Claims (6)

対象物質を含む液体と、吸着剤とを接触させて、前記液体に含まれる前記対象物質を選択的に前記吸着剤に吸着させて、前記液体から除去する工程を含む、液体の清浄化方法であって、
前記吸着剤が、亜鉛イオンまたはコバルトイオンと、2−メチルイミダゾレート配位子とからなるゼオライト型イミダゾレート骨格である金属有機構造体を含む、液体の清浄化方法。
A liquid cleaning method comprising a step of bringing a liquid containing a target substance into contact with an adsorbent, selectively adsorbing the target substance contained in the liquid to the adsorbent, and removing the target substance from the liquid. There,
A method for cleaning a liquid, wherein the adsorbent includes a metal organic structure that is a zeolite type imidazolate skeleton composed of zinc ions or cobalt ions and a 2-methylimidazolate ligand.
前記対象物質が、含酸素有機化合物または芳香族化合物である、請求項1に記載の液体の清浄化方法。   The method for cleaning a liquid according to claim 1, wherein the target substance is an oxygen-containing organic compound or an aromatic compound. 前記対象物質が、含酸素六員環化合物またはフェノール性水酸基を有する芳香族化合物である、請求項1または2に記載の液体の清浄化方法。   The method for cleaning a liquid according to claim 1 or 2, wherein the target substance is an oxygen-containing six-membered ring compound or an aromatic compound having a phenolic hydroxyl group. 前記対象物質が、1,4−ジオキサン、テトラヒドロピラン、フェノール、ベンゼンまたはトルエンである、請求項1乃至3のいずれかに記載の液体の清浄化方法。   The liquid cleaning method according to claim 1, wherein the target substance is 1,4-dioxane, tetrahydropyran, phenol, benzene, or toluene. 前記液体が、水溶液または有機溶液である、請求項1乃至4のいずれかに記載の液体の清浄化方法。   The liquid cleaning method according to claim 1, wherein the liquid is an aqueous solution or an organic solution. 金属有機構造体を含む吸着剤であって、
前記金属有機構造体が、亜鉛イオンと2−メチルイミダゾレート配位子とからなるゼオライト型イミダゾレート骨格であり、
当該吸着剤が、液体中の対象物質を選択的に吸着する、吸着剤。
An adsorbent comprising a metal-organic structure,
The metal organic structure is a zeolite type imidazolate skeleton composed of zinc ions and 2-methylimidazolate ligands;
An adsorbent that selectively adsorbs a target substance in a liquid.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20210041412A (en) * 2019-10-07 2021-04-15 국방과학연구소 Absorbent comprising zeolitic imidazolate framework for absorbing chemical warfare agents and application thereof
WO2021261376A1 (en) * 2020-06-23 2021-12-30 株式会社村田製作所 Electrochemical device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20210041412A (en) * 2019-10-07 2021-04-15 국방과학연구소 Absorbent comprising zeolitic imidazolate framework for absorbing chemical warfare agents and application thereof
KR102278739B1 (en) * 2019-10-07 2021-07-20 국방과학연구소 Absorbent comprising zeolitic imidazolate framework for absorbing chemical warfare agents and application thereof
WO2021261376A1 (en) * 2020-06-23 2021-12-30 株式会社村田製作所 Electrochemical device
JP7424488B2 (en) 2020-06-23 2024-01-30 株式会社村田製作所 electrochemical device

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