JP6471256B1 - Deodorizing material and deodorizing sheet - Google Patents

Deodorizing material and deodorizing sheet Download PDF

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JP6471256B1
JP6471256B1 JP2018095797A JP2018095797A JP6471256B1 JP 6471256 B1 JP6471256 B1 JP 6471256B1 JP 2018095797 A JP2018095797 A JP 2018095797A JP 2018095797 A JP2018095797 A JP 2018095797A JP 6471256 B1 JP6471256 B1 JP 6471256B1
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deodorizing material
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博規 藤木
博規 藤木
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Unitika Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0262Compounds of O, S, Se, Te
    • B01J20/0266Compounds of S
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0274Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
    • B01J20/0281Sulfates of compounds other than those provided for in B01J20/045
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s

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  • Chemical Kinetics & Catalysis (AREA)
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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

【課題】優れたアセトアルデヒド吸着性能を効率良く発揮する脱臭材を提供する。
【解決手段】活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、
前記活性炭は、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上である、脱臭材。
【選択図】 なし
[PROBLEMS] To provide a deodorizing material that efficiently exhibits excellent acetaldehyde adsorption performance.
SOLUTION: An activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine, or (B) an aromatic amine, a sulfate of the aromatic amine, and a sulfuric acid supported on the activated carbon. Including deodorizing material,
The activated carbon is a deodorizing material having a pore volume of 0.6 cc / g or more and a pore volume of 0.65 nm or more and 2.0 nm or less.
[Selection figure] None

Description

本発明は、脱臭材及び脱臭シートに関する。   The present invention relates to a deodorizing material and a deodorizing sheet.

近年、空気浄化に関する関心が高まっており、室内等において、より悪臭の少ない環境が求められている。また、シックハウス症候群の問題を発端として、住環境における揮発性有機化合物(VOC)への対策も求められている。   In recent years, there has been an increasing interest in air purification, and there is a demand for an environment with less offensive odor in a room or the like. In addition, starting from the problem of sick house syndrome, countermeasures against volatile organic compounds (VOC) in the living environment are also required.

例えば、自動車などの車室内においては、シートパッド、インストルメント・パネル、ドアトリムなどの内装樹脂部品、塗料、接着剤などからの揮発性有機化合物の悪臭、さらに、排気ガス、燃料臭、タバコ、人体、食品の腐敗物などの多くの悪臭が発生し得る。また、車室内は、住宅に比して空間が狭いため、密閉すると特に悪臭が充満しやすいという問題を有する。   For example, in vehicle interiors such as automobiles, bad odors of volatile organic compounds from interior resin parts such as seat pads, instrument panels, door trims, paints, adhesives, exhaust gases, fuel odors, tobacco, human bodies, etc. Many bad odors, such as food rots, can occur. Further, since the interior of the vehicle interior is narrower than that of a house, there is a problem that a bad odor tends to be filled when sealed.

特許文献1は、繊維状活性炭と芳香族アミノ酸と硫酸とを含んだ繊維状脱臭材であって、以下の工程を含む方法によって製造された繊維状脱臭材を開示している。
芳香族アミノ酸と硫酸とを含有した水溶液中に繊維状活性炭を浸漬させて繊維状活性炭に芳香族アミノ酸と硫酸とを担持させる工程であって、繊維状活性炭に対する芳香族アミノ酸の質量比を10質量%乃至20質量%の範囲内とし、繊維状活性炭に対する硫酸の質量比を5質量%乃至25質量%の範囲内とする工程と、
芳香族アミノ酸及び硫酸を担持させた繊維状活性炭から水溶液を除去する工程と、
水溶液を除去した繊維状活性炭を乾燥させる工程。
Patent document 1 is a fibrous deodorizing material containing fibrous activated carbon, an aromatic amino acid, and sulfuric acid, and discloses a fibrous deodorizing material produced by a method including the following steps.
A step of immersing a fibrous activated carbon in an aqueous solution containing an aromatic amino acid and sulfuric acid to allow the fibrous activated carbon to carry the aromatic amino acid and sulfuric acid, wherein the mass ratio of the aromatic amino acid to the fibrous activated carbon is 10 mass. % To 20% by mass, and the step of making the mass ratio of sulfuric acid to fibrous activated carbon 5% to 25% by mass;
Removing the aqueous solution from the fibrous activated carbon carrying the aromatic amino acid and sulfuric acid;
A step of drying the fibrous activated carbon from which the aqueous solution has been removed.

特開2011−72603号公報JP 2011-72603 A

本発明者は、特許文献1に開示された脱臭材において、活性炭に芳香族アミノ酸と硫酸を担持させることによるアセトアルデヒドの吸着性能を、より効率良く発揮させたいと考えた。すなわち、活性炭に同じ量の芳香族アミノ酸と硫酸を担持させた場合に、アセトアルデヒド吸着性能をより向上させることを考えた。   The present inventor wanted to make the deodorizing material disclosed in Patent Document 1 exhibit more efficiently the adsorption performance of acetaldehyde by supporting an aromatic amino acid and sulfuric acid on activated carbon. That is, it was considered to improve the acetaldehyde adsorption performance when the same amount of aromatic amino acid and sulfuric acid were supported on activated carbon.

そこで、本発明は、上記問題を解決し、同じ浸漬条件において活性炭に芳香族アミノ酸と硫酸とを担持させて脱臭材とした場合に、脱臭材のアセトアルデヒド吸着性能を効率良く発揮させる、脱臭材を提供することを主な目的とする。   Accordingly, the present invention provides a deodorizing material that solves the above-mentioned problems and efficiently exhibits the acetaldehyde adsorption performance of the deodorizing material when the activated carbon is loaded with an aromatic amino acid and sulfuric acid on the same immersion conditions to form a deodorizing material. The main purpose is to provide.

本発明者は、このような課題を解決するために鋭意検討を行った。その結果、芳香族アミノ酸と硫酸を、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上とした活性炭、に担持させた場合、同じ浸漬条件で芳香族アミノ酸と硫酸を、上記活性炭以外の活性炭、すなわち、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g未満の活性炭、に担持させた場合に比して、優れたアセトアルデヒド吸着性能を発揮することを見出した。本発明は、これらの知見に基づいて、さらに検討を重ねることにより完成された発明である。   The present inventor has intensively studied to solve such problems. As a result, when the aromatic amino acid and sulfuric acid were supported on activated carbon having a pore volume of 0.65 nm or more and 2.0 nm or less and a pore volume of 0.6 cc / g or more, Excellent acetaldehyde adsorption compared to the case where sulfuric acid is supported on activated carbon other than the above activated carbon, that is, activated carbon having a pore volume of 0.65 nm or more and 2.0 nm or less and a pore volume of less than 0.6 cc / g. It has been found that it demonstrates its performance. The present invention has been completed by further studies based on these findings.

すなわち、本発明は、下記に掲げる態様の発明を提供する。
項1. 活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、
前記活性炭は、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上である、脱臭材。
項2. 前記活性炭は、全細孔容積(cc/g)が前記0.65nm以上2.0nm以下の細孔径の細孔容積の1〜2倍である、項1の脱臭材。
項3. 前記活性炭の3nm以上の細孔径の細孔容積が0.02cc/g以下である、項1又は2に記載の脱臭材。
項4. 前記活性炭の比表面積が1500m2/g以上である、項1〜3のいずれか1項に記載の脱臭材。
項5. 前記脱臭材の比表面積が400〜1200m2/gである、項1〜4のいずれか1項に記載の脱臭材。
項6. 前記活性炭の比表面積から前記脱臭材の比表面積を減じた値が800〜1300m2/gである、項1〜5のいずれか1項に記載の脱臭材。
項7. 平衡濃度10ppmにおけるアセトアルデヒドの平衡吸着量(mg/gACF)が35mg/gACF以上である、項1〜6のいずれか1項に記載の脱臭材。
項8. 項1〜7のいずれか1項に記載の脱臭材を含む、脱臭シート。
That is, this invention provides the invention of the aspect hung up below.
Item 1. A deodorizing material comprising activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine, or (B) an aromatic amine, a sulfate of the aromatic amine, and sulfuric acid supported on the activated carbon. Because
The activated carbon is a deodorizing material having a pore volume of 0.6 cc / g or more and a pore volume of 0.65 nm or more and 2.0 nm or less.
Item 2. Item 2. The deodorizing material according to Item 1, wherein the activated carbon has a total pore volume (cc / g) of 1 to 2 times the pore volume of the pore diameter of 0.65 nm to 2.0 nm.
Item 3. Item 3. The deodorizing material according to Item 1 or 2, wherein the activated carbon has a pore volume of a pore diameter of 3 nm or more of 0.02 cc / g or less.
Item 4. Item 4. The deodorizing material according to any one of Items 1 to 3, wherein the activated carbon has a specific surface area of 1500 m 2 / g or more.
Item 5. Item 5. The deodorizing material according to any one of Items 1 to 4, wherein the deodorizing material has a specific surface area of 400 to 1200 m 2 / g.
Item 6. Item 6. The deodorizing material according to any one of Items 1 to 5, wherein a value obtained by subtracting the specific surface area of the deodorizing material from the specific surface area of the activated carbon is 800 to 1300 m 2 / g.
Item 7. Item 7. The deodorizing material according to any one of Items 1 to 6, wherein an equilibrium adsorption amount (mg / g ACF) of acetaldehyde at an equilibrium concentration of 10 ppm is 35 mg / g ACF or more.
Item 8. Item 8. A deodorizing sheet comprising the deodorizing material according to any one of items 1 to 7.

本発明の脱臭材は、活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、前記活性炭が、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上であることから、優れたアセトアルデヒド吸着性能を効率良く発揮することができる。また、本発明の脱臭材を含む脱臭シートも、優れたアセトアルデヒド吸着性能を効率良く発揮することができる。   The deodorizing material of the present invention comprises activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine supported on the activated carbon, or (B) an aromatic amine, a sulfate of the aromatic amine, and A deodorizing material containing sulfuric acid, wherein the activated carbon has a pore volume of 0.6 cc / g or more and a pore diameter of 0.6 nm or more and 2.0 nm or less, and has excellent acetaldehyde adsorption performance efficiently. It can be demonstrated. Moreover, the deodorizing sheet containing the deodorizing material of this invention can also exhibit the outstanding acetaldehyde adsorption performance efficiently.

本発明の脱臭材は、活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、前記活性炭は、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上であることを特徴とする。以下、本発明の脱臭材及びこれを用いた脱臭シートについて詳述する。   The deodorizing material of the present invention comprises activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine supported on the activated carbon, or (B) an aromatic amine, a sulfate of the aromatic amine, and A deodorizing material containing sulfuric acid, wherein the activated carbon has a pore volume of 0.6 cc / g or more and a pore diameter of 0.65 nm or more and 2.0 nm or less. Hereinafter, the deodorizing material of the present invention and the deodorizing sheet using the same will be described in detail.

以下において、細孔容積とは、QSDFT法(急冷固体密度汎関数法)によって算出される細孔容積をいう。QSDFT法とは、幾何学的・化学的に不規則なミクロポーラス・メソポーラスな炭素の細孔径解析を対象とした、約0.5nm〜約40nmまでの細孔径分布の計算ができる解析手法である。QSDFT法では、細孔表面の粗さと不均一性による影響が明瞭に考慮されているため、細孔径分布解析の正確さが大幅に向上した手法である。本発明においては、Quantachrome社製「AUTOSORB−1−MP」を用いて窒素吸着等温線の測定、及びQSDFT法による細孔径分布解析をおこなう。77Kの温度において測定した窒素の脱着等温線に対し、Calculation modelとしてN2 at 77K on carbon[slit pore,QSDFT equilibrium model]を適用して細孔径分布を計算することで、特定の細孔径範囲の細孔容積を算出することができる。   Hereinafter, the pore volume refers to the pore volume calculated by the QSDFT method (quenched solid density functional method). The QSDFT method is an analytical method capable of calculating a pore size distribution from about 0.5 nm to about 40 nm for geometrically and chemically irregular microporous and mesoporous carbon pore size analysis. . In the QSDFT method, the influence of the roughness and nonuniformity of the pore surface is clearly taken into account, so that the accuracy of the pore diameter distribution analysis is greatly improved. In the present invention, measurement of nitrogen adsorption isotherm and pore size distribution analysis by QSDFT method are performed using “AUTOSORB-1-MP” manufactured by Quantachrome. By applying N2 at 77K on carbon [slit pore, QSDFT equilibrium model] as a calibration model to the nitrogen desorption isotherm measured at a temperature of 77 K, the pore size distribution is calculated to obtain a fine pore size range. The pore volume can be calculated.

本発明の脱臭材は、活性炭と、(A)「芳香族アミン及び該芳香族アミンの硫酸塩」、又は、(B)「芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸」とを含む。本発明の脱臭材において、活性炭と、芳香族アミン及び該芳香族アミンの硫酸塩とが含まれる場合には、(A)芳香族アミン及び該芳香族アミンの硫酸塩が、当該活性炭に担持されている。また、本発明の脱臭材において、活性炭と、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とが含まれる場合には、芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸が、当該活性炭に担持されている。   The deodorizing material of the present invention comprises activated carbon and (A) “aromatic amine and sulfate of the aromatic amine” or (B) “aromatic amine, sulfate of the aromatic amine, and sulfuric acid”. Including. In the deodorizing material of the present invention, when activated carbon, an aromatic amine and a sulfate of the aromatic amine are included, (A) the aromatic amine and the sulfate of the aromatic amine are supported on the activated carbon. ing. When the deodorizing material of the present invention contains activated carbon and (B) an aromatic amine, a sulfate of the aromatic amine, and sulfuric acid, the aromatic amine, the sulfate of the aromatic amine, and Sulfuric acid is supported on the activated carbon.

本発明の脱臭材において、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸(以下、総称して「本発明の脱臭材に含まれる薬剤」と略することがある。)を担持させる、活性炭は、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上である。このような特定の細孔分布を有する活性炭を用いることにより、優れたアセトアルデヒド吸着性能を効率良く発揮することができる。   In the deodorizing material of the present invention, (A) an aromatic amine and a sulfate of the aromatic amine, or (B) an aromatic amine, a sulfate of the aromatic amine, and sulfuric acid (hereinafter collectively referred to as “the present invention”). The activated carbon that carries "the chemical contained in the deodorizing material") has a pore volume of 0.6 cc / g or more with a pore diameter of 0.65 nm or more and 2.0 nm or less. By using activated carbon having such a specific pore distribution, excellent acetaldehyde adsorption performance can be efficiently exhibited.

本発明の脱臭材において、上記特定の細孔分布を有する活性炭を用いることにより優れたアセトアルデヒド吸着性能を効率良く発揮する理由としては、次のようなことが考えられる。すなわち、アセトアルデヒドは分子サイズが小さいため、これを吸着する活性炭の細孔としては、小さいものが好ましいとも考えられた。しかしながら、本発明の脱臭材に含まれる薬剤は、本発明者の検討によれば、活性炭の0.65〜2.0nmの範囲の細孔径に担持されやすいことが明らかとなった。より具体的に、上記薬剤担持前と担持後の活性炭細孔分布を調べたところ、0.65〜2.0nmの範囲の細孔容積の減少率が高かった。このことは、あらゆる細孔径の中でも、当該範囲の細孔径の細孔内に上記薬剤がより多く担持されることを示すと考えられる。そこで、上記特定の細孔分布を有する活性炭を用いることにより、上記薬剤を細孔内に担持しやすくして、細孔による吸着効果と、上記薬剤の細孔内担持による薬剤とアセトアルデヒドとの接触面積向上効果と、の相乗効果が生じやすくなり、結果、優れたアセトアルデヒド吸着性能を効率良く発揮できると考えられる。   In the deodorizing material of the present invention, the reason why the acetaldehyde adsorbing performance excellent by using the activated carbon having the specific pore distribution can be efficiently exhibited is as follows. That is, since acetaldehyde has a small molecular size, it was considered that small pores are preferable as the pores of activated carbon that adsorbs acetaldehyde. However, it has become clear that the drug contained in the deodorizing material of the present invention is easily supported by the pore diameter in the range of 0.65 to 2.0 nm of activated carbon according to the study of the present inventors. More specifically, when the activated carbon pore distribution before and after the drug loading was examined, the rate of decrease in the pore volume in the range of 0.65 to 2.0 nm was high. This is considered to indicate that a larger amount of the drug is supported in pores having a pore diameter in the above range among all pore diameters. Therefore, by using activated carbon having the specific pore distribution, it is easy to support the drug in the pores, the adsorption effect by the pores, and the contact between the drug and acetaldehyde by the support of the drug in the pores. It is likely that a synergistic effect with the area improvement effect is likely to occur, and as a result, excellent acetaldehyde adsorption performance can be efficiently exhibited.

上記0.65nm以上2.0nm以下の細孔径の細孔容積は、アセトアルデヒド吸着性能をより一層効率よく発揮する観点から、0.7cc/g以上が好ましく、0.75cc/g以上がより好ましい。また、当該細孔容積の上限値は特に制限されないが、例えば、1.2cc/g以下が挙げられ、1.0cc/g以下が挙げられる。なお、本明細書において、活性炭の説明については、別途説明の無い限り、本発明の脱臭材に含まれる薬剤を担持する前のものを示す。   The pore volume having a pore diameter of 0.65 nm or more and 2.0 nm or less is preferably 0.7 cc / g or more, more preferably 0.75 cc / g or more, from the viewpoint of more efficiently exhibiting acetaldehyde adsorption performance. Moreover, although the upper limit of the pore volume is not particularly limited, for example, 1.2 cc / g or less is exemplified, and 1.0 cc / g or less is exemplified. In the present specification, unless otherwise specified, the description of the activated carbon is the one before carrying the chemical contained in the deodorizing material of the present invention.

本発明の脱臭材において、活性炭の全細孔容積は、0.65nm以上2.0nm以下の細孔径の細孔容積を確保しつつ、アセトアルデヒドの吸着性能をより向上させる観点から、0.65nm以上2.0nm以下の細孔径の細孔容積の1〜2倍程度、好ましくは1.1〜1.4倍程度が挙げられる。具体的には、例えば、0.7〜2.0cc/gが挙げられ、0.7〜1.2cc/gが好ましく挙げられる。   In the deodorizing material of the present invention, the total pore volume of the activated carbon is 0.65 nm or more from the viewpoint of further improving the acetaldehyde adsorption performance while ensuring a pore volume having a pore diameter of 0.65 nm or more and 2.0 nm or less. About 1-2 times the pore volume with a pore diameter of 2.0 nm or less, preferably about 1.1-1.4 times. Specifically, 0.7-2.0 cc / g is mentioned, for example, 0.7-1.2 cc / g is mentioned preferably.

本発明の脱臭材において、活性炭の、全細孔容積に対する0.65nm以上2.0nm以下の細孔径の細孔容積の割合(0.65nm以上2.0nm以下の細孔径の細孔容積/全細孔容積)としては、例えば、0.6〜0.9が挙げられ、0.7〜0.85が好ましく挙げられ、0.7〜0.75がより好ましく挙げられる。   In the deodorizing material of the present invention, the ratio of the pore volume of the pore diameter of 0.65 nm to 2.0 nm to the total pore volume of the activated carbon (pore volume of the pore diameter of 0.65 nm to 2.0 nm / total Examples of the pore volume include 0.6 to 0.9, preferably 0.7 to 0.85, and more preferably 0.7 to 0.75.

本発明の脱臭材において、活性炭の、2nm以下の細孔径の細孔容積としては、0.65nm以上2.0nm以下の細孔径の細孔容積を確保しつつ、アセトアルデヒドの吸着性能をより向上させる観点から、例えば、0.7〜0.9cc/gが好ましく挙げられ、0.85〜0.9cc/gがより好ましく挙げられる。また、全細孔容積に対する2nm以下の細孔径の細孔容積の割合(2nm以下の細孔径の細孔容積/全細孔容積)としては、同様の観点から、0.8〜0.98が好ましく挙げられ、0.80〜0.85がより好ましく挙げられる。   In the deodorizing material of the present invention, as the pore volume of activated carbon with a pore diameter of 2 nm or less, the acetaldehyde adsorption performance is further improved while ensuring a pore volume with a pore diameter of 0.65 nm or more and 2.0 nm or less. From the viewpoint, for example, 0.7 to 0.9 cc / g is preferable, and 0.85 to 0.9 cc / g is more preferable. Further, the ratio of the pore volume having a pore diameter of 2 nm or less to the total pore volume (pore volume of pore diameter of 2 nm or less / total pore volume) is 0.8 to 0.98 from the same viewpoint. Preferred examples are 0.80 to 0.85.

本発明の脱臭材において、活性炭の、0.65nm以下の細孔径の細孔容積としては、0.65nm以上2.0nm以下の細孔径の細孔容積を確保しつつ、アセトアルデヒドの吸着性能をより向上させる観点から、例えば、0.05〜0.12cc/gが好ましく挙げられ、0.08〜0.1cc/gがより好ましく挙げられる。また、全細孔容積に対する0.65nm以下の細孔径の細孔容積の割合(0.65nm以下の細孔径の細孔容積/全細孔容積)としては、同様の観点から、0.05〜0.20が好ましく挙げられ、0.05〜0.12がより好ましく挙げられる。   In the deodorizing material of the present invention, the activated carbon has a pore volume of 0.65 nm or less with a pore volume of 0.65 nm or less and a pore volume of 0.65 nm or more and 2.0 nm or less, while further increasing the acetaldehyde adsorption performance. From the viewpoint of improving, for example, 0.05 to 0.12 cc / g is preferable, and 0.08 to 0.1 cc / g is more preferable. Further, the ratio of the pore volume having a pore diameter of 0.65 nm or less to the total pore volume (pore volume of pore diameter of 0.65 nm or less / total pore volume) is 0.05 to 0.20 is mentioned preferably and 0.05-0.12 is mentioned more preferably.

本発明の脱臭材において、活性炭の、2nm以上3nm以下の細孔径の細孔容積としては、0.65nm以上2.0nm以下の細孔径の細孔容積を確保しつつ、アセトアルデヒドの吸着性能をより向上させる観点から、0.01〜0.2cc/gが好ましく挙げられ、0.15〜0.2cc/gがより好ましく挙げられる。また、全細孔容積に対する2nm以上3nm以下の細孔径の細孔容積の割合(2nm以上3nm以下の細孔径の細孔容積/全細孔容積)としては、同様の観点から、0.01〜0.20が好ましく挙げられ、0.15〜0.20がより好ましく挙げられる。   In the deodorizing material of the present invention, as the pore volume of the activated carbon having a pore diameter of 2 nm or more and 3 nm or less, the acetaldehyde adsorption performance is improved while ensuring the pore volume of the pore diameter of 0.65 nm or more and 2.0 nm or less. From a viewpoint of improving, 0.01-0.2 cc / g is mentioned preferably and 0.15-0.2 cc / g is mentioned more preferably. The ratio of the pore volume having a pore diameter of 2 nm or more and 3 nm or less to the total pore volume (pore volume of pore diameter of 2 nm or more and 3 nm or less / total pore volume) is 0.01 to 0.20 is mentioned preferably and 0.15-0.20 is mentioned more preferably.

本発明の脱臭材において、活性炭の、3nm以上の細孔径の細孔容積としては、0.65nm以上2.0nm以下の細孔径の細孔容積を確保しつつ、当該範囲の細孔径により多くの本発明の脱臭材に含まれる薬剤を担持させやすくする観点から、0.02cc/g以下が好ましく挙げられ、0.01cc/g以下がより好ましく挙げられる。   In the deodorizing material of the present invention, the pore volume of the activated carbon with a pore diameter of 3 nm or more is secured to a pore volume with a pore diameter of 0.65 nm or more and 2.0 nm or less, and more From the viewpoint of facilitating loading of the chemical contained in the deodorizing material of the present invention, it is preferably 0.02 cc / g or less, more preferably 0.01 cc / g or less.

本発明の脱臭材において、活性炭の比表面積としては、0.65nm以上2.0nm以下の細孔径の細孔容積を確保しつつ、アセトアルデヒド吸着性能をより優れたものとする観点から、1500m2/g以上が好ましく、1900m2/g以上がより好ましい。上限値は特に制限されないが、例えば、3500m2/g以下が挙げられ、2500m2/g以下が挙げられる。活性炭の比表面積は、JIS K1477に記載されたBET法(1点法)により求めた値である。 In the deodorizing material of the present invention, the specific surface area of the activated carbon is 1500 m 2 / from the viewpoint of improving the acetaldehyde adsorption performance while ensuring a pore volume having a pore diameter of 0.65 nm to 2.0 nm. g or more is preferable, and 1900 m 2 / g or more is more preferable. Although an upper limit is not restrict | limited in particular, For example, 3500 m < 2 > / g or less is mentioned, For example, 2500 m < 2 > / g or less is mentioned. The specific surface area of the activated carbon is a value determined by the BET method (one-point method) described in JIS K1477.

本発明の脱臭材において、活性炭の形態は特に限定されないが、例えば、粒状活性炭、粉末状活性炭、繊維状活性炭等が挙げられる。アセトアルデヒドの吸着速度が比較的速いという観点からは、繊維状である繊維状活性炭とすることがより好ましい。なお、繊維状活性炭の平均繊維径としては、好ましくは30μm以下、より好ましくは5〜20μm程度が挙げられる。なお、本発明における平均繊維径は、画像処理繊維径測定装置(JIS K 1477に準拠)により測定した値である。また、粒状活性炭及び粉末状活性炭の粒径としては、レーザー回折/散乱式法で測定した積算体積百分率D50が0.01〜5mmが挙げられる。   In the deodorizing material of the present invention, the form of activated carbon is not particularly limited, and examples thereof include granular activated carbon, powdered activated carbon, and fibrous activated carbon. From the viewpoint that the adsorption rate of acetaldehyde is relatively fast, it is more preferable to use fibrous activated carbon that is fibrous. In addition, as an average fiber diameter of fibrous activated carbon, Preferably it is 30 micrometers or less, More preferably, about 5-20 micrometers is mentioned. In addition, the average fiber diameter in this invention is the value measured with the image processing fiber diameter measuring apparatus (based on JISK1477). Moreover, as a particle size of granular activated carbon and powdered activated carbon, the integrated volume percentage D50 measured by the laser diffraction / scattering type method is 0.01-5 mm.

活性炭前駆体の原料種及び形態としては特に制限されるものではない。活性炭前駆体の原料種の例としては、不融化或いは炭素化した有機質材料、フェノール樹脂等の硬化性樹脂等が挙げられ、該有機質材料としては、例えば、ポリアクリロニトリル、ピッチ、ポリビニルアルコール、セルロース等が挙げられる。また、オガ屑、木材チップ、木材、ピート、木炭、ヤシ殻、石炭、オイル、炭素質物質(石油コークス、石炭コークス、石油ピッチ、石炭ピッチ、コールタールピッチ、及びこれらの複合物など)、合成樹脂(フェノール樹脂、ポリアクリロニトリル(PAN)、ポリイミド、フラン樹脂など)、セルロース系繊維(紙、綿繊維など)、及びこれらの複合物(紙−フェノール樹脂積層板など)、フラーレンなどが挙げられる。これらの中でも、炭素化時の理論炭素化収率の点で、ピッチであることが好ましく、石炭ピッチであることがより好ましい。活性炭前駆体の形態の例としては、粒状、粉末状、繊維状等が挙げられる。   The raw material species and form of the activated carbon precursor are not particularly limited. Examples of the raw material species of the activated carbon precursor include infusible or carbonized organic materials, curable resins such as phenol resins, and the like, for example, polyacrylonitrile, pitch, polyvinyl alcohol, cellulose, etc. Is mentioned. Also sawdust, wood chips, wood, peat, charcoal, coconut husk, coal, oil, carbonaceous materials (petroleum coke, coal coke, petroleum pitch, coal pitch, coal tar pitch, and composites thereof), synthesis Examples thereof include resins (phenol resins, polyacrylonitrile (PAN), polyimides, furan resins, etc.), cellulosic fibers (paper, cotton fibers, etc.), and composites thereof (paper-phenol resin laminates, etc.), fullerenes, and the like. Among these, in terms of the theoretical carbonization yield at the time of carbonization, pitch is preferable, and coal pitch is more preferable. Examples of the form of the activated carbon precursor include granular, powdery, and fibrous forms.

本発明の脱臭材に用いる活性炭を得る方法としては、特に制限されないが、例えば、上記活性炭前駆体を、水蒸気を用いて、所定の細孔分布となるよう、賦活温度、賦活時間を調整して得る方法が挙げられる。   The method for obtaining the activated carbon used for the deodorizing material of the present invention is not particularly limited. For example, the activated carbon precursor is adjusted by using steam to adjust the activation temperature and activation time so as to have a predetermined pore distribution. The method of obtaining is mentioned.

本発明の脱臭材において、芳香族アミンとしては特に制限されないがアセトアルデヒドの他、トルエン及びアンモニアに対する脱臭能をより効果的に高めるため、また製造上の取り扱い易さや安全上の観点から、ハロゲン、スルホ基、アセトアミド基、又はカルボニル基がベンゼン環に結合した芳香族アミンが好ましい。ハロゲン、スルホ基、アセトアミド基、又はカルボニル基がベンゼン環に結合した芳香族アミンとしては、アミノ安息香酸、アミノアセトアニリド、アミノサリチル酸、アミノスルファニル酸等が好ましく挙げられる。中でも、芳香族アミンと該芳香族アミンの硫酸塩としてはアミノ安息香酸及びその硫酸塩が好ましい。すなわち、本発明の脱臭材においては、繊維状活性炭にアミノ安息香酸及びその硫酸塩が担持されていることが好ましい。本発明の脱臭材中において、芳香族アミンの少なくとも一部は、後述の硫酸と共に硫酸塩を形成する。芳香族アミンと該芳香族アミンの硫酸塩は、1種類単独で使用してもよいし、2種類以上を組み合わせて使用してもよい。   In the deodorizing material of the present invention, the aromatic amine is not particularly limited, but in order to more effectively enhance the deodorizing ability with respect to toluene and ammonia in addition to acetaldehyde, and from the viewpoint of ease of handling in production and safety, halogen, sulfo An aromatic amine in which a group, an acetamide group or a carbonyl group is bonded to a benzene ring is preferred. Preferred examples of the aromatic amine having a halogen, a sulfo group, an acetamide group, or a carbonyl group bonded to a benzene ring include aminobenzoic acid, aminoacetanilide, aminosalicylic acid, and aminosulfanilic acid. Among these, aminobenzoic acid and its sulfate are preferable as the aromatic amine and the sulfate of the aromatic amine. That is, in the deodorizing material of the present invention, it is preferred that aminobenzoic acid and its sulfate are supported on fibrous activated carbon. In the deodorizing material of the present invention, at least a part of the aromatic amine forms a sulfate with sulfuric acid described later. The aromatic amine and the sulfate of the aromatic amine may be used alone or in combination of two or more.

アミノ安息香酸としては、特に制限されず、p−アミノ安息香酸、m−アミノ安息香酸、及びo−アミノ安息香酸のうち少なくとも1種を用いることができる。アセトアルデヒドの他、トルエン及びアンモニアに対する脱臭能をより効果的に高める観点からは、本発明の脱臭材においては、p−アミノ安息香酸が担持されていることが特に好ましい。   The aminobenzoic acid is not particularly limited, and at least one of p-aminobenzoic acid, m-aminobenzoic acid, and o-aminobenzoic acid can be used. In addition to acetaldehyde, it is particularly preferable that p-aminobenzoic acid is supported in the deodorizing material of the present invention from the viewpoint of more effectively increasing the deodorizing ability with respect to toluene and ammonia.

本発明の脱臭材においては、上記の芳香族アミンと該芳香族アミンの硫酸塩と共に、硫酸が担持されていてもよい。すなわち、本発明の脱臭材は、(A)芳香族アミンと該芳香族アミンの硫酸塩が担持された活性炭(硫酸が担持されていなくてもよい)、又は、(B)芳香族アミンと該芳香族アミンの硫酸塩と硫酸とが担持された活性炭を備えている。   In the deodorizing material of this invention, a sulfuric acid may be carry | supported with said aromatic amine and sulfate of this aromatic amine. That is, the deodorizing material of the present invention comprises (A) an activated carbon on which an aromatic amine and a sulfate of the aromatic amine are supported (sulfuric acid may not be supported), or (B) an aromatic amine and the An activated carbon on which an aromatic amine sulfate and sulfuric acid are supported is provided.

硫酸は、沸点が比較的高く、揮発し難い。硫酸は、水へのアミノ安息香酸の溶解を促進するため、後述するような脱臭材の製造過程において、活性炭に芳香族アミンと該芳香族アミンの硫酸塩を均一に担持させることを可能とする。さらに、硫酸は、脱臭材において、芳香族アミン、芳香族アミンの硫酸塩同士が互いに重合することを抑制する効果を発揮する。   Sulfuric acid has a relatively high boiling point and is difficult to volatilize. Sulfuric acid promotes the dissolution of aminobenzoic acid in water, so that it is possible to uniformly carry an aromatic amine and a sulfate of the aromatic amine on activated carbon in the process of producing a deodorizing material as described later. . Furthermore, sulfuric acid exhibits the effect of suppressing the polymerization of aromatic amines and sulfates of aromatic amines in the deodorizing material.

本発明の脱臭材において、芳香族アミンと該芳香族アミンの硫酸塩の合計担持量としては、特に制限されないが、例えば、活性炭100質量部に対し、10〜40質量部とすることが挙げられ、アセトアルデヒド吸着性能をより高める観点から、20〜40質量部が好ましく挙げられ、25〜35質量部がより好ましく挙げられる。また、本発明の脱臭材において、芳香族アミンの硫酸塩と硫酸の合計担持量としては、特に制限されないが、例えば、活性炭100質量部に対し、0.5〜5質量部とすることが挙げられ、2〜5質量部とすることが好ましく挙げられる。   In the deodorizing material of the present invention, the total supported amount of the aromatic amine and the sulfate of the aromatic amine is not particularly limited, and for example, it may be 10 to 40 parts by mass with respect to 100 parts by mass of the activated carbon. From the viewpoint of further improving the acetaldehyde adsorption performance, 20 to 40 parts by mass are preferably exemplified, and 25 to 35 parts by mass are more preferably exemplified. Moreover, in the deodorizing material of the present invention, the total supported amount of the sulfate and sulfuric acid of the aromatic amine is not particularly limited, but for example, it may be 0.5 to 5 parts by mass with respect to 100 parts by mass of the activated carbon. Preferably, the content is 2 to 5 parts by mass.

本発明の脱臭材の比表面積(本発明の脱臭材に含まれる薬剤を担持後の比表面積)としては、特に制限されないが、例えば、400〜1200m2/gが挙げられ、500〜1100m2/gが好ましく挙げられ、700〜1100m2/gがより好ましく挙げられる。また、当該比表面積は、例えば、900〜1200m2/gであり得るし、500〜800m2/gであり得る。 Although it does not restrict | limit especially as a specific surface area (specific surface area after carrying | supporting the chemical | medical agent contained in the deodorizing material of this invention) of the deodorizing material of this invention, For example, 400-1200 m < 2 > / g is mentioned, 500-1100 m < 2 > / g>. g is preferable, and 700 to 1100 m 2 / g is more preferable. Further, the specific surface area, for example, be a 900~1200m 2 / g, may be 500~800m 2 / g.

本発明の脱臭材において、本発明の脱臭材に含まれる薬剤の担持により減少する比表面積(=担持前の活性炭の比表面積−担持後の脱臭材の比表面積)としては、例えば、800〜1300m2/gが挙げられ、900〜1200m2/gが挙げられる。また、本発明の脱臭材において、活性炭の比表面積の、本発明の脱臭材に含まれる薬剤の担持による減少率(=担持後の脱臭材の比表面積/担持前の活性炭の比表面積×100(%))としては、例えば、30〜60%が挙げられる。 In the deodorizing material of the present invention, the specific surface area (= specific surface area of activated carbon before supporting−specific surface area of the deodorizing material after supporting) reduced by loading of the chemical contained in the deodorizing material of the present invention is, for example, 800 to 1300 m. 2 / g is mentioned, and 900-1200 m < 2 > / g is mentioned. Further, in the deodorizing material of the present invention, the reduction rate of the specific surface area of the activated carbon due to the loading of the drug contained in the deodorizing material of the present invention (= specific surface area of the deodorizing material after loading / specific surface area of the activated carbon before loading × 100 ( %)) Includes, for example, 30 to 60%.

本発明の脱臭材において、平衡濃度10ppmにおけるアセトアルデヒドの平衡吸着量(mg/gACF)としては、好ましくは35mg/gACF以上、より好ましくは45〜70mg/gACF、特に好ましくは50〜60mg/gACFが挙げられる。なお、本発明の脱臭材の平衡濃度10ppmにおけるアセトアルデヒドの平衡吸着量の測定方法は、それぞれ、以下の通りである。   In the deodorizing material of the present invention, the equilibrium adsorption amount (mg / g ACF) of acetaldehyde at an equilibrium concentration of 10 ppm is preferably 35 mg / g ACF or more, more preferably 45 to 70 mg / g ACF, particularly preferably 50 to 60 mg / g ACF. It is done. In addition, the measuring method of the equilibrium adsorption amount of acetaldehyde in the equilibrium concentration of 10 ppm of the deodorizing material of the present invention is as follows.

(アセトアルデヒドの平衡吸着量の測定)
任意重量の試料片と100ppmアセトアルデヒドガス3Lを密閉容器に封入し、25℃の環境下において静置する。24時間経過後、容器内のガス濃度を測定し、吸着量を計算する。複数の試料重量について測定を行い、それぞれの計算結果より、濃度と吸着量の相関をグラフにプロットし、得られた関係式より、任意の平衡濃度におけるアセトアルデヒドの平衡吸着量(mg/gACF)を導く。アセトアルデヒドの濃度測定には、ガスクロマトグラフィー、またはガス検知管を用いる。
(Measurement of equilibrium adsorption amount of acetaldehyde)
A sample piece of an arbitrary weight and 3 L of 100 ppm acetaldehyde gas are sealed in a sealed container and allowed to stand in an environment of 25 ° C. After 24 hours, the gas concentration in the container is measured and the amount of adsorption is calculated. Measure the weight of multiple samples, plot the correlation between concentration and adsorption amount on the graph from each calculation result, and calculate the equilibrium adsorption amount (mg / g ACF) of acetaldehyde at any equilibrium concentration from the obtained relational expression. Lead. Gas chromatography or a gas detector tube is used for measuring the concentration of acetaldehyde.

本発明の脱臭材は、例えば、次のようにして製造することができる。まず、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上である活性炭を準備する。当該活性炭を得る方法としては、前述のとおりである。次に、芳香族アミンおよび/またはその塩と、硫酸および/またはその塩と、水とを含有した処理液を調製する。芳香族アミンおよび/またはその塩は、水で十分に希釈した硫酸および/またはその塩の水溶液中に溶解させてもよく、硫酸および/またはその塩を比較的高い濃度で含んだ水溶液中に溶解させた後にこれを水で希釈して処理液としてもよい。硫酸としては、濃硫酸を用いてもよいし、希硫酸を用いてもよい。また、芳香族アミンおよび/またはその塩を水に溶解させるために、硫酸および/またはその塩の水溶液を、例えば50〜80℃の範囲内の温度に加熱し、ここに芳香族アミンおよび/またはその塩を混合してもよい。また、芳香族アミンとしては、前述のものを用いる。芳香族アミンの塩としては、特に制限されないが、例えば、当該芳香族アミンの硫酸塩などが挙げられる。   The deodorizing material of this invention can be manufactured as follows, for example. First, activated carbon having a pore volume of 0.65 nm or more and 2.0 nm or less and a pore volume of 0.6 cc / g or more is prepared. The method for obtaining the activated carbon is as described above. Next, a treatment liquid containing an aromatic amine and / or salt thereof, sulfuric acid and / or salt thereof, and water is prepared. Aromatic amines and / or salts thereof may be dissolved in an aqueous solution of sulfuric acid and / or its salt sufficiently diluted with water, and dissolved in an aqueous solution containing sulfuric acid and / or its salt at a relatively high concentration. Then, it may be diluted with water to form a treatment liquid. As sulfuric acid, concentrated sulfuric acid or dilute sulfuric acid may be used. Also, in order to dissolve the aromatic amine and / or salt thereof in water, an aqueous solution of sulfuric acid and / or salt thereof is heated to a temperature in the range of, for example, 50 to 80 ° C., where the aromatic amine and / or The salt may be mixed. As the aromatic amine, those described above are used. Although it does not restrict | limit especially as a salt of an aromatic amine, For example, the sulfate of the said aromatic amine etc. are mentioned.

処理液における芳香族アミンおよび/またはその塩の仕込み量としては、本発明の脱臭材における芳香族アミンおよび/またはその塩の担持量が所望の範囲となるように設定すれば、特に制限されず、例えば、後に浸漬する活性炭100質量部に対して、12〜40質量部程度とすればよい。また、処理液における硫酸および/またはその塩の仕込み量としては、本発明の脱臭材における芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸の含有量が所望の範囲となるように設定すれば、特に制限されず、後に浸漬する活性炭100質量部に対して、12〜40質量部程度とすればよい。   The amount of the aromatic amine and / or salt thereof charged in the treatment liquid is not particularly limited as long as the amount of the aromatic amine and / or salt thereof in the deodorizing material of the present invention is set within a desired range. For example, what is necessary is just to set it as about 12-40 mass parts with respect to 100 mass parts of activated carbon immersed later. In addition, the amount of sulfuric acid and / or salt thereof charged in the treatment liquid may be selected from the aromatic amine and sulfate of the aromatic amine, or the aromatic amine and sulfate of sulfuric acid and sulfuric acid in the deodorizing material of the present invention. If it sets so that content of may become a desired range, it will not restrict | limit in particular, What is necessary is just about 12-40 mass parts with respect to 100 mass parts of activated carbon to immerse later.

次に、この処理液中に準備した活性炭を浸漬して、該活性炭に芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸を担持させる。例えば、活性炭を処理液中に均一に分散させ、その後、十分な時間に亘ってこの分散液を静置する。活性炭を処理液中に浸漬させる時間は、例えば約1時間以上とする。活性炭の質量と処理液の体積との比は、例えば5〜50g/Lの範囲内とする。この比が小さすぎる場合、芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸を活性炭に担持させるためにより長い時間を要する。一方、この比が大きすぎる場合、芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸を活性炭に均一に担持させることが難しくなる。なお、活性炭を水溶液と接触させている時間が十分に長ければ、この比が活性炭に担持される芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸の量に及ぼす影響は無視することができる。なお、活性炭を浸漬する処理液は、上記の芳香族アミンおよび/またはその塩の仕込みの際に加熱された状態で使用してもよく、加熱した処理液を冷却した後に使用してもよい。   Next, the activated carbon prepared is immersed in the treatment liquid, and the activated amine carries the aromatic amine and the sulfate of the aromatic amine, or the aromatic amine, the sulfate of the aromatic amine, and the sulfuric acid. For example, activated carbon is uniformly dispersed in the treatment liquid, and then this dispersion liquid is allowed to stand for a sufficient time. The time for immersing the activated carbon in the treatment liquid is, for example, about 1 hour or more. The ratio between the mass of the activated carbon and the volume of the treatment liquid is, for example, in the range of 5 to 50 g / L. When this ratio is too small, it takes a longer time to support the aromatic amine and the sulfate of the aromatic amine, or the aromatic amine, the sulfate of the aromatic amine and the sulfuric acid on the activated carbon. On the other hand, when this ratio is too large, it becomes difficult to uniformly carry the aromatic amine and the sulfate of the aromatic amine, or the aromatic amine, the sulfate of the aromatic amine and the sulfuric acid on the activated carbon. If the time for which the activated carbon is in contact with the aqueous solution is sufficiently long, this ratio is the aromatic amine supported on the activated carbon and the sulfate of the aromatic amine, or the aromatic amine and the sulfate of the aromatic amine. The effect on the amount of sulfuric acid is negligible. In addition, the processing liquid which immerses activated carbon may be used in the state heated at the time of preparation of said aromatic amine and / or its salt, and may be used after cooling the heated processing liquid.

次いで、芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸とを担持させた活性炭から処理液を除去する。処理液を除去する方法としては、特に制限されず、例えば、活性炭を処理液から引き上げることにより行うことができる。芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸とを担持させた活性炭からの処理液の除去に先立って、処理液を水で希釈してもよい。   Next, the treatment liquid is removed from the activated carbon on which the aromatic amine and the sulfate of the aromatic amine or the aromatic amine, the sulfate of the aromatic amine and the sulfuric acid are supported. The method for removing the treatment liquid is not particularly limited, and can be performed, for example, by pulling up activated carbon from the treatment liquid. Prior to the removal of the treatment liquid from the aromatic amine and the sulfate of the aromatic amine or the activated liquid carrying the aromatic amine, the sulfate of the aromatic amine and the sulfuric acid, the treatment liquid is diluted with water. May be.

その後、処理液を除去した活性炭を乾燥させる。この乾燥には、例えば、自然乾燥、通風乾燥、熱風乾燥、マイクロ波加熱乾燥、間接加熱乾燥などを利用することができる。乾燥は、活性炭の温度が、例えば130℃以下、好ましくは80℃以下に維持されるように行う。以上のようにして、本発明の脱臭材を製造することができる。   Thereafter, the activated carbon from which the treatment liquid has been removed is dried. For this drying, for example, natural drying, ventilation drying, hot air drying, microwave heating drying, indirect heating drying, or the like can be used. Drying is performed so that the temperature of the activated carbon is maintained at, for example, 130 ° C. or lower, preferably 80 ° C. or lower. As described above, the deodorizing material of the present invention can be produced.

次に、本発明の脱臭シートについて詳述する。本発明の脱臭シートは、上記の本発明の脱臭材を用いたものであり、本発明の脱臭材を含む。具体的には、本発明の脱臭シートは、例えば、上記の脱臭材がシート状に成形されたものである。シートの形態としては、特に限定されないが、不織布が好ましく挙げられる。本発明の脱臭シートは、上記の脱臭材をシート状に成形することなどを目的として、必要に応じてバインダーを含んでいてもよい。バインダーとしては、脱臭材を構成する活性炭同士を接着できるものであれば特に制限されず、例えば、(繊維状バインダーが挙げられ、繊維状バインダーの市販品としてはユニチカ株式会社製商品名メルティ)などを使用することができる。   Next, the deodorizing sheet of the present invention will be described in detail. The deodorizing sheet of the present invention uses the above-described deodorizing material of the present invention, and includes the deodorizing material of the present invention. Specifically, the deodorizing sheet of the present invention is, for example, a sheet in which the above-mentioned deodorizing material is formed. Although it does not specifically limit as a form of a sheet | seat, A nonwoven fabric is mentioned preferably. The deodorizing sheet of this invention may contain the binder as needed for the purpose of shape | molding said deodorizing material in a sheet form. The binder is not particularly limited as long as the activated carbon constituting the deodorizing material can be bonded to each other. For example, (a fibrous binder is mentioned, and a commercial product of fibrous binder is trade name Melty manufactured by Unitika Ltd.) Can be used.

本発明の脱臭シートがバインダーを含む場合、バインダーと、本発明の脱臭材との質量比(バインダー/脱臭材)としては、好ましくは75/25〜25/75程度が挙げられる。また、後述する、脱臭シートの密度を低いものとする場合には、アセトアルデヒドに対する脱臭能をより一層優れたものとすることから、活性炭の質量割合を少ないものとしやすくなり、例えば、バインダーと本発明の脱臭材との質量比(バインダー/脱臭材)としては、75/25〜65/35程度としやすくなる。   When the deodorizing sheet of the present invention contains a binder, the mass ratio (binder / deodorizing material) between the binder and the deodorizing material of the present invention is preferably about 75/25 to 25/75. Further, when the density of the deodorizing sheet to be described later is low, the deodorizing ability with respect to acetaldehyde is further improved, so that the mass ratio of the activated carbon is easily reduced, for example, the binder and the present invention. As a mass ratio (binder / deodorizing material) to the deodorizing material, it becomes easy to be about 75/25 to 65/35.

本発明の脱臭シートの密度は、特に限定されるものではないが、アセトアルデヒドに対する脱臭能をより一層優れたものとする観点から、例えば、0.05〜0.3g/cm3が好ましく、0.05〜0.20g/cm3がより好ましく、0.08〜0.15g/cm3が特に好ましい。また、本発明の脱臭シートの厚さとしては、例えば、0.15〜0.80mm、好ましくは0.3〜0.7mmとすると、上記脱臭能に優れつつ、車室内の座席のカバー内に収容できやすくなる。上記のような密度が低い、および/または薄いシートを得る方法としては、例えば、目付け1〜8g/m2程度の薄い不織布を製造し、該不織布を複数層重ねてニードルパンチ加工を施して一体化させることにより得ることができる。 The density of the deodorizing sheet of the present invention is not particularly limited, but is preferably, for example, 0.05 to 0.3 g / cm 3 from the viewpoint of further improving the deodorizing ability with respect to acetaldehyde. 05 to 0.20 g / cm 3 is more preferable, and 0.08 to 0.15 g / cm 3 is particularly preferable. In addition, the thickness of the deodorizing sheet of the present invention is, for example, 0.15 to 0.80 mm, preferably 0.3 to 0.7 mm. It becomes easy to accommodate. As a method for obtaining a sheet having a low density and / or a thinness as described above, for example, a thin nonwoven fabric having a basis weight of about 1 to 8 g / m 2 is manufactured, and a plurality of the nonwoven fabrics are stacked and subjected to needle punch processing to be integrated. Can be obtained.

本発明の脱臭シートは、例えば、上記の脱臭材をシート状に成形することにより製造することもできるし、繊維状活性炭に芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸を担持させる前の繊維状活性炭をシート状に成形した後、当該シートを上記と同様にして処理液に浸漬して、繊維状活性炭に芳香族アミンと該芳香族アミンの硫酸塩、又は、芳香族アミンと該芳香族アミンの硫酸塩と硫酸を担持させることによっても製造することができる。   The deodorizing sheet of the present invention can be produced, for example, by molding the above-mentioned deodorizing material into a sheet shape, and an aromatic amine and a sulfate of the aromatic amine or an aromatic amine on a fibrous activated carbon. After forming the fibrous activated carbon before supporting the sulfate and sulfuric acid of the aromatic amine into a sheet, the sheet is immersed in a treatment solution in the same manner as described above, and the aromatic amine and the aromatic are added to the fibrous activated carbon. It can also be produced by supporting an aromatic amine sulfate or an aromatic amine, an aromatic amine sulfate and sulfuric acid.

本発明の脱臭シートを空気浄化用シートとして用いる場合は、エレクトレット化された不織布シート、HEPA(high efficiency particulate air)フィルタ、ULPA(ultra low penetration air)フィルタなどの除塵シートを脱臭シートに貼り合せることによって、除塵効果を付与した積層体とすることも可能である。そのような積層体は、空気浄化と除塵とを行う空気清浄器などにおいて好適に使用され得る。   When the deodorizing sheet of the present invention is used as an air purification sheet, a dust removing sheet such as an electret nonwoven sheet, a high efficiency particulate air (HEPA) filter, or an ULPA (ultra low penetration air) filter is pasted on the deodorizing sheet. Thus, it is possible to obtain a laminated body having a dust removal effect. Such a laminate can be suitably used in an air purifier that performs air purification and dust removal.

本発明の脱臭シートは、上記した本発明の脱臭材を含んでいるため、アセトアルデヒドを、高い効率で気相から除去することができる。従って、本発明の脱臭シートは、住環境において広く使用することができ、自動車、電車、船舶、飛行機などの内装材にも好適に使用できる。中でも、本発明の脱臭シートは、アセトアルデヒドを、高い効率で気相から除去できる自動車内装材として、車室内の座席のカバー内に収容して用いることができる。すなわち、本発明の脱臭シートを含む、車室内用座席とすることができる。また、本発明の脱臭材は、アセトアルデヒド以外にも、ホルムアルデヒド等の低級アルデヒドに対しても、脱臭能を有する。   Since the deodorizing sheet of the present invention contains the above-described deodorizing material of the present invention, acetaldehyde can be removed from the gas phase with high efficiency. Therefore, the deodorizing sheet of the present invention can be widely used in a living environment, and can also be suitably used for interior materials such as automobiles, trains, ships and airplanes. Especially, the deodorizing sheet of this invention can be accommodated and used in the cover of the seat of a vehicle interior as a motor vehicle interior material which can remove acetaldehyde from a gaseous phase with high efficiency. That is, it can be set as a vehicle interior seat including the deodorizing sheet of the present invention. Moreover, the deodorizing material of this invention has a deodorizing ability also with respect to lower aldehydes, such as formaldehyde, besides acetaldehyde.

以下に、実施例及び比較例を示して本発明を詳細に説明する。ただし、本発明は、実施例に限定されない。   Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples. However, the present invention is not limited to the examples.

[試験例A]
<実施例1A>
活性炭の準備
粒状石炭ピッチを、溶融押出機に供給し、溶融温度320℃で溶融混合し、吐出量20g/minで紡糸することによりピッチ繊維を得た。得られたピッチ繊維を空気中常温から354℃まで1〜30℃/分の割合で54分間昇温することにより不融化処理をおこない、不融化されたピッチ繊維である活性炭前駆体を得た。得られた活性炭前駆体を、H2O濃度が100容量%のガスを賦活炉内に連続的に導入し、雰囲気温度875℃で70分間熱処理することにより賦活をおこない、繊維状活性炭を得た。得られた繊維状活性炭の0.65nm以上2.0nm以下の細孔径の細孔容積は0.781cc/gであった。また、全細孔容積は1.058cc/g、2nm以下の細孔径の細孔容積は0.877cc/g、比表面積は2069m2/g、0.65nm以下の細孔径の細孔容積は0.096cc/g、2nm以上3nm以下の細孔径の細孔容積は0.174cc/g、3nm以上の細孔径の細孔容積は0.007cc/gであった。なお、実施例において、2nm以上3nm以下の細孔径の細孔容積は、3nm以下の細孔径の細孔容積を求め、当該細孔容積から、上記2nm以下の細孔径の細孔容積を減ずることにより求めた。また、3nm以上の細孔径の細孔容積は、上記全細孔容積から、上記3nm以下の細孔径の細孔容積を減ずることにより求めた。
[Test Example A]
<Example 1A>
Preparation of activated carbon Granular coal pitch was supplied to a melt extruder, melted and mixed at a melting temperature of 320 ° C., and spun at a discharge rate of 20 g / min to obtain pitch fibers. The pitch fiber thus obtained was heated in the air at a rate of 1 to 30 ° C./min for 54 minutes from room temperature to 354 ° C. to obtain an activated carbon precursor which was an infusible pitch fiber. The obtained activated carbon precursor was activated by continuously introducing a gas having an H 2 O concentration of 100% by volume into an activation furnace and heat-treating it at an ambient temperature of 875 ° C. for 70 minutes to obtain fibrous activated carbon. . The obtained fibrous activated carbon had a pore volume of 0.781 cc / g with a pore diameter of 0.65 nm to 2.0 nm. The total pore volume is 1.058 cc / g, the pore volume of 2 nm or less is 0.877 cc / g, the specific surface area is 2069 m 2 / g, and the pore volume of 0.65 nm or less is 0. The pore volume of pore diameters of 0.096 cc / g and 2 nm or more and 3 nm or less was 0.174 cc / g, and the pore volume of pore diameters of 3 nm or more was 0.007 cc / g. In Examples, the pore volume having a pore diameter of 2 nm or more and 3 nm or less is obtained by subtracting the pore volume having a pore diameter of 2 nm or less from the pore volume. Determined by The pore volume having a pore diameter of 3 nm or more was determined by subtracting the pore volume having a pore diameter of 3 nm or less from the total pore volume.

本発明の脱臭材に含まれる薬剤溶液Aの調製
まず、75質量%の濃度で硫酸を含有した硫酸水溶液を調製した。この硫酸水溶液を65℃以上の温度で撹拌して、芳香族アミンとしてp−アミノ安息香酸を水溶液に加え、完全に溶解させたのち、活性炭の質量と処理液の体積との比が20g/Lとなるように水を加え、処理液を得た。なお、芳香族アミン及び硫酸の仕込み量は、活性炭100質量部に対して15.0質量部となるようにした。なお、硫酸の当該仕込み量(質量部)は、75質量%硫酸水溶液中の、純水を除いた硫酸のみの量(質量部)を示す。
Preparation of drug solution A contained in deodorizing material of the present invention First, an aqueous sulfuric acid solution containing sulfuric acid at a concentration of 75% by mass was prepared. After stirring this sulfuric acid aqueous solution at a temperature of 65 ° C. or more and adding p-aminobenzoic acid as an aromatic amine to the aqueous solution and completely dissolving it, the ratio of the mass of activated carbon to the volume of the treatment liquid is 20 g / L. Water was added to obtain a treatment solution. The amount of aromatic amine and sulfuric acid charged was 15.0 parts by mass with respect to 100 parts by mass of activated carbon. In addition, the said preparation amount (mass part) of a sulfuric acid shows the quantity (mass part) of only the sulfuric acid except a pure water in 75 mass% sulfuric acid aqueous solution.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、薬剤溶液Aに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、実施例1Aの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、以下のようにして測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution A. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain the deodorizing material of Example 1A. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( (Mass part) was measured as follows.

活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)の測定
活性炭に担持された芳香族アミンと該芳香族アミンの硫酸塩の合計担持量については、薬剤溶液の、活性炭を浸漬する前の液と活性炭を浸漬した後の液の有機物濃度を、それぞれ全有機物濃度(TOC)計を用いて測定し、浸漬操作前後の有機物濃度の差から、合計担持量を測定した。具体的には、まず全有機物濃度(TOC)計(株式会社島津製作所製TOC−5000)を用いて、浸漬操作前後の薬剤溶液について、炭素(C)に換算された有機物濃度(mgC/L)を測定し、操作前後の濃度の差を求めた。別途、秤量して調製した既知濃度の芳香族アミン水溶液について同様に全有機物濃度を測定し、有機物濃度(mgC/L)と芳香族アミン濃度(mg芳香族アミン/L)の対応を表す検量線を作成した。作成した検量線を用いて、添着操作前後の有機物濃度の差(mgC/L)を芳香族アミン濃度の差(mg芳香族アミン/L)に換算した。求めた濃度の差に処理液量(L)を乗じて芳香族アミン質量の差を算出した。算出された値を、薬剤溶液に浸漬する前の活性炭100質量部あたりの質量部に換算し、得られた質量部を、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)とした。
Measurement of total supported amount (mass part) of aromatic amine and sulfate of aromatic amine with respect to 100 parts by mass of activated carbon About the total supported amount of aromatic amine and sulfate of aromatic amine supported on activated carbon, Measure the organic concentration of the solution before immersing the activated carbon and the concentration after immersing the activated carbon using a total organic concentration (TOC) meter. From the difference in organic concentration before and after the immersing operation, the total supported amount Was measured. Specifically, first, using a total organic matter concentration (TOC) meter (TOC-5000 manufactured by Shimadzu Corporation), the concentration of organic matter (mgC / L) converted to carbon (C) for the drug solution before and after the dipping operation. And the difference in concentration before and after the operation was determined. Separately, weighed and prepared a known concentration of aromatic amine aqueous solution to measure the total organic matter concentration in the same manner, and a calibration curve representing the correspondence between the organic matter concentration (mgC / L) and the aromatic amine concentration (mg aromatic amine / L). It was created. Using the prepared calibration curve, the difference (mg C / L) in the organic matter concentration before and after the attaching operation was converted to the difference in the aromatic amine concentration (mg aromatic amine / L). The difference in aromatic amine mass was calculated by multiplying the determined concentration difference by the amount of processing solution (L). The calculated value is converted into mass parts per 100 parts by mass of activated carbon before being immersed in the drug solution, and the obtained mass part is the sum of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of activated carbon. The supported amount (parts by mass) was used.

活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)の測定
活性炭に担持された芳香族アミンの硫酸塩と硫酸の合計物質量についても同様に、活性炭を浸漬する前の薬剤溶液と、活性炭を浸漬した後の薬剤溶液について、JIS K 0101:1998 42.4に規定のイオンクロマトグラフ法に準じ硫酸イオンの濃度(mg/L)を測定することで、これらの合計担持量を計算した。具体的には浸漬操作前後の薬剤溶液の硫酸イオンの濃度(mg/L)を、検量線を用いてそれぞれ測定し、操作前後の硫酸イオン濃度の差(mg/L)を求めた。求めた操作前後の硫酸イオン濃度の差(mg/L)に、硫酸の分子量(98.08g/mol)と硫酸イオンの分子量(96.06g/mol)の比を乗じて硫酸濃度の差に換算した。硫酸濃度の差に処理液量(L)を乗じて操作前後の硫酸の差を算出した。算出した操作前後の硫酸の差を、薬剤溶液に浸漬する前の活性炭100質量部あたりの質量部に換算し、得られた質量部を、活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)とした。
Measurement of Total Amount of Aromatic Amine Sulfate and Sulfuric Acid (Mass Part) with respect to 100 parts by Mass of Activated Carbon The same applies to the total amount of aromatic amine sulfate and sulfuric acid supported on activated carbon before immersing the activated carbon. The concentration of sulfate ion (mg / L) was measured in accordance with the ion chromatographic method specified in JIS K 0101: 1998 42.4 for the drug solution after immersion in activated carbon and the drug solution after the activated carbon was immersed. The loading was calculated. Specifically, the sulfate ion concentration (mg / L) of the drug solution before and after the dipping operation was measured using a calibration curve, and the difference in sulfate ion concentration before and after the operation (mg / L) was determined. Multiply the difference in sulfate ion concentration before and after the operation (mg / L) by the ratio between the molecular weight of sulfuric acid (98.08 g / mol) and the molecular weight of sulfate ion (96.06 g / mol) to convert to the difference in sulfuric acid concentration. did. The difference in sulfuric acid before and after the operation was calculated by multiplying the difference in sulfuric acid concentration by the amount of processing solution (L). The calculated difference in sulfuric acid before and after the operation was converted to mass parts per 100 parts by mass of activated carbon before immersing in the drug solution, and the obtained mass parts were obtained by using an aromatic amine sulfate and sulfuric acid with respect to 100 parts by mass of activated carbon. The total supported amount (parts by mass) was used.

<比較例1A>
活性炭の準備
粒状石炭ピッチを、溶融押出機に供給し、溶融温度320℃で溶融混合し、吐出量20g/minで紡糸することによりピッチ繊維を得た。得られたピッチ繊維を空気中常温から354℃まで1〜30℃/分の割合で54分間昇温することにより不融化処理をおこない、不融化されたピッチ繊維である活性炭前駆体を得た。得られた活性炭前駆体を、H2O濃度が100容量%のガスを賦活炉内に連続的に導入し、雰囲気温度875℃で30分間熱処理することにより賦活をおこない、繊維状活性炭を得た。得られた繊維状活性炭の0.65nm以上2.0nm以下の細孔径の細孔容積は0.116cc/gであった。また、全細孔容積は0.315cc/g、2nm以下の細孔径の細孔容積は0.315cc/g、比表面積は825m2/g、0.65nm以下の細孔径の細孔容積は0.199cc/g、2nm以上3nm以下の細孔径の細孔容積は0.000cc/g、3nm以上の細孔径の細孔容積は0.000cc/gであった。
<Comparative Example 1A>
Preparation of activated carbon Granular coal pitch was supplied to a melt extruder, melted and mixed at a melting temperature of 320 ° C., and spun at a discharge rate of 20 g / min to obtain pitch fibers. The pitch fiber thus obtained was heated in the air at a rate of 1 to 30 ° C./min for 54 minutes from room temperature to 354 ° C. to obtain an activated carbon precursor which was an infusible pitch fiber. The obtained activated carbon precursor was activated by continuously introducing a gas having an H 2 O concentration of 100% by volume into an activation furnace and heat-treating it at an ambient temperature of 875 ° C. for 30 minutes to obtain a fibrous activated carbon. . The resulting fibrous activated carbon had a pore volume of 0.116 cc / g with a pore diameter of 0.65 nm to 2.0 nm. Further, the total pore volume is 0.315 cc / g, the pore volume of 2 nm or less is 0.315 cc / g, the specific surface area is 825 m 2 / g, and the pore volume of 0.65 nm or less is 0. 199 cc / g The pore volume of pore diameters of 2 nm or more and 3 nm or less was 0.000 cc / g, and the pore volume of pore diameters of 3 nm or more was 0.000 cc / g.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Aで準備した薬剤溶液Aに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例1Aの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution A prepared in Example 1A. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 1A. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例2A>
活性炭の準備
粒状石炭ピッチを、溶融押出機に供給し、溶融温度320℃で溶融混合し、吐出量20g/minで紡糸することによりピッチ繊維を得た。得られたピッチ繊維を空気中常温から354℃まで1〜30℃/分の割合で54分間昇温することにより不融化処理をおこない、不融化されたピッチ繊維である活性炭前駆体を得た。得られた活性炭前駆体を、H2O濃度が100容量%のガスを賦活炉内に連続的に導入し、雰囲気温度875℃で40分間熱処理することにより賦活をおこない、繊維状活性炭を得た。得られた繊維状活性炭の0.65nm以上2.0nm以下の細孔径の細孔容積は0.255cc/gであった。また、全細孔容積は0.476cc/g、2nm以下の細孔径の細孔容積は0.476cc/g、比表面積は1232m2/g、0.65nm以下の細孔径の細孔容積は0.211cc/g、2nm以上3nm以下の細孔径の細孔容積は0.000cc/g、3nm以上の細孔径の細孔容積は0.000cc/gであった。
<Comparative Example 2A>
Preparation of activated carbon Granular coal pitch was supplied to a melt extruder, melted and mixed at a melting temperature of 320 ° C., and spun at a discharge rate of 20 g / min to obtain pitch fibers. The pitch fiber thus obtained was heated in the air at a rate of 1 to 30 ° C./min for 54 minutes from room temperature to 354 ° C. to obtain an activated carbon precursor which was an infusible pitch fiber. The obtained activated carbon precursor was activated by continuously introducing a gas having an H 2 O concentration of 100% by volume into an activation furnace and heat treating it at an ambient temperature of 875 ° C. for 40 minutes to obtain a fibrous activated carbon. . The resulting fibrous activated carbon had a pore volume of 0.255 cc / g with a pore diameter of 0.65 nm to 2.0 nm. The total pore volume is 0.476 cc / g, the pore volume of 2 nm or less is 0.476 cc / g, the specific surface area is 1232 m 2 / g, and the pore volume of 0.65 nm or less is 0. 0.21 cc / g, the pore volume having a pore diameter of 2 nm or more and 3 nm or less was 0.000 cc / g, and the pore volume having a pore diameter of 3 nm or more was 0.000 cc / g.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Aで準備した薬剤溶液Aに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例2Aの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution A prepared in Example 1A. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 2A. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例3A>
活性炭の準備
有機質材料として、軟化点が280℃の粒状石炭ピッチ100質量部に対してトリスアセチルアセトナトイットリウム1.3質量部を混合したものを、溶融押出機に供給し、溶融温度320℃で溶融混合し、吐出量20g/minで紡糸することによりピッチ繊維を得た。得られたピッチ繊維を空気中常温から354℃まで1〜30℃/分の割合で54分間昇温することにより不融化処理をおこない、不融化されたピッチ繊維である活性炭前駆体を得た。得られた活性炭前駆体を、H2O濃度が100容量%のガスを賦活炉内に連続的に導入し、雰囲気温度900℃で20分間熱処理することにより賦活をおこない、繊維状活性炭を得た。得られた繊維状活性炭の0.65nm以上2.0nm以下の細孔径の細孔容積は0.335cc/gであった。また、全細孔容積は0.572cc/g、2nm以下の細孔径の細孔容積は0.395cc/g、比表面積は1078m2/g、0.65nm以下の細孔径の細孔容積は0.075cc/g、2nm以上3nm以下の細孔径の細孔容積は0.113cc/g、3nm以上の細孔径の細孔容積は0.050cc/gであった。
<Comparative Example 3A>
Preparation of activated carbon As an organic material, a mixture of 1.3 parts by mass of trisacetylacetonatoyttrium with 100 parts by mass of granular coal pitch with a softening point of 280 ° C. is supplied to a melt extruder at a melting temperature of 320 ° C. Pitch fibers were obtained by melt mixing and spinning at a discharge rate of 20 g / min. The pitch fiber thus obtained was heated in the air at a rate of 1 to 30 ° C./min for 54 minutes from room temperature to 354 ° C. to obtain an activated carbon precursor which was an infusible pitch fiber. The obtained activated carbon precursor was activated by continuously introducing a gas having an H 2 O concentration of 100% by volume into an activation furnace and heat-treating it at an ambient temperature of 900 ° C. for 20 minutes to obtain a fibrous activated carbon. . The obtained fibrous activated carbon had a pore volume of a pore diameter of 0.65 nm to 2.0 nm of 0.335 cc / g. Also, the total pore volume is 0.572 cc / g, the pore volume of 2 nm or less is 0.395 cc / g, the specific surface area is 1078 m 2 / g, and the pore volume of 0.65 nm or less is 0. The pore volume of pore diameters of 0.075 cc / g, 2 nm or more and 3 nm or less was 0.113 cc / g, and the pore volume of pore diameters of 3 nm or more was 0.050 cc / g.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Aで準備した薬剤溶液Aに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例3Aの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution A prepared in Example 1A. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 3A. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

実施例1A、比較例1A〜3Aで得た脱臭材を用い、比表面積、アセトアルデヒド平衡吸着量を前述の方法に従い、測定した。また、得られた脱臭材の比表面積から活性炭の比表面積を減じ、芳香族アミン及び硫酸の担持により減少した比表面積を算出した。また、上記アセトアルデヒド平衡吸着量は、比較例2Aの平衡吸着量を1としたときの比で評価した。結果を表1に示す。   Using the deodorizing materials obtained in Example 1A and Comparative Examples 1A to 3A, the specific surface area and the acetaldehyde equilibrium adsorption amount were measured according to the methods described above. Further, the specific surface area of the activated carbon was subtracted from the specific surface area of the obtained deodorizing material, and the specific surface area decreased due to the loading of the aromatic amine and sulfuric acid was calculated. Moreover, the said acetaldehyde equilibrium adsorption amount was evaluated by the ratio when the equilibrium adsorption amount of Comparative Example 2A was 1. The results are shown in Table 1.

Figure 0006471256
Figure 0006471256

<試験例Aの小括>
実施例1Aは、活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、前記活性炭が、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上であることから、同じ浸漬条件で芳香族アミノ酸と硫酸を、上記活性炭以外の活性炭、すなわち、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g未満の比較例1A〜3Aの活性炭、に担持させた場合に比して、優れたアセトアルデヒド吸着性能を発揮するものであった。
<Summary of Test Example A>
Example 1A includes activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine, or (B) an aromatic amine, a sulfate of the aromatic amine, and sulfuric acid supported on the activated carbon. The activated carbon has a pore volume of 0.65 nm to 2.0 nm in pore diameter of 0.6 cc / g or more, so that the aromatic amino acid and sulfuric acid are used under the same immersion conditions. In comparison with the case where the activated carbon other than the activated carbon, that is, the activated carbon of Comparative Examples 1A to 3A having a pore volume of 0.65 nm or more and 2.0 nm or less and a pore volume of less than 0.6 cc / g, It exhibited excellent acetaldehyde adsorption performance.

[試験例B]
<実施例1B>
活性炭の準備
実施例1Aで得た活性炭を準備した。
[Test Example B]
<Example 1B>
Preparation of activated carbon The activated carbon obtained in Example 1A was prepared.

本発明の脱臭材に含まれる薬剤溶液Bの調製
まず、75質量%の濃度で硫酸を含有した硫酸水溶液を調製した。この硫酸水溶液を65℃以上の温度で撹拌して、芳香族アミンとしてp−アミノ安息香酸を水溶液に加え、完全に溶解させたのち、活性炭の質量と処理液の体積との比が20g/Lとなるように水を加え、処理液を得た。なお、芳香族アミン及び硫酸の仕込み量は、活性炭100質量部に対して22.5質量部となるようにした。なお、硫酸の当該仕込み量(質量部)は、75硫酸水溶液中の、純水を除いた硫酸のみの量(質量部)を示す。
Preparation of drug solution B contained in deodorizing material of the present invention First, a sulfuric acid aqueous solution containing sulfuric acid at a concentration of 75% by mass was prepared. After stirring this sulfuric acid aqueous solution at a temperature of 65 ° C. or more and adding p-aminobenzoic acid as an aromatic amine to the aqueous solution and completely dissolving it, the ratio of the mass of activated carbon to the volume of the treatment liquid is 20 g / L. Water was added to obtain a treatment solution. The amount of the aromatic amine and sulfuric acid charged was 22.5 parts by mass with respect to 100 parts by mass of the activated carbon. In addition, the said preparation amount (mass part) of a sulfuric acid shows the quantity (mass part) of only the sulfuric acid except a pure water in 75 sulfuric acid aqueous solution.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、薬剤溶液Bに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、実施例1Bの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution B. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain the deodorizing material of Example 1B. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<実施例2B>
活性炭の準備
粒状石炭ピッチを、溶融押出機に供給し、溶融温度320℃で溶融混合し、吐出量20g/minで紡糸することによりピッチ繊維を得た。得られたピッチ繊維を空気中常温から354℃まで1〜30℃/分の割合で54分間昇温することにより不融化処理をおこない、不融化されたピッチ繊維である活性炭前駆体を得た。得られた活性炭前駆体を、H2O濃度が100容量%のガスを賦活炉内に連続的に導入し、雰囲気温度875℃で50分間熱処理することにより賦活をおこない、繊維状活性炭を得た。得られた繊維状活性炭の0.65nm以上2.0nm以下の細孔径の細孔容積は0.622cc/gであった。また、全細孔容積は0.753cc/g、2nm以下の細孔径の細孔容積は0.728cc/g、比表面積は1731m2/g、0.65nm以下の細孔径の細孔容積は0.106cc/g、2nm以上3nm以下の細孔径の細孔容積は0.025cc/g、3nm以上の細孔径の細孔容積は0.000cc/gであった。
<Example 2B>
Preparation of activated carbon Granular coal pitch was supplied to a melt extruder, melted and mixed at a melting temperature of 320 ° C., and spun at a discharge rate of 20 g / min to obtain pitch fibers. The pitch fiber thus obtained was heated in the air at a rate of 1 to 30 ° C./min for 54 minutes from room temperature to 354 ° C. to obtain an activated carbon precursor which was an infusible pitch fiber. The obtained activated carbon precursor was activated by continuously introducing a gas having an H 2 O concentration of 100% by volume into an activation furnace and heat treating it at an ambient temperature of 875 ° C. for 50 minutes to obtain fibrous activated carbon. . The fibrous activated carbon obtained had a pore volume of 0.622 cc / g with a pore diameter of 0.65 nm to 2.0 nm. The total pore volume is 0.753 cc / g, the pore volume of 2 nm or less is 0.728 cc / g, the specific surface area is 1731 m 2 / g, and the pore volume of 0.65 nm or less is 0. The pore volume of pore diameters of .106 cc / g, 2 nm or more and 3 nm or less was 0.025 cc / g, and the pore volume of pore diameters of 3 nm or more was 0.000 cc / g.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Bで準備した薬剤溶液Bに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、実施例2Bの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution B prepared in Example 1B. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain the deodorizing material of Example 2B. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例1B>
活性炭の準備
比較例1Aで得た活性炭を準備した。
<Comparative Example 1B>
Preparation of activated carbon The activated carbon obtained in Comparative Example 1A was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Bで準備した薬剤溶液Bに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例1Bの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution B prepared in Example 1B. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 1B. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例2B>
活性炭の準備
比較例2Aで得た活性炭を準備した。
<Comparative Example 2B>
Preparation of activated carbon The activated carbon obtained in Comparative Example 2A was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Bで準備した薬剤溶液Bに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例2Bの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution B prepared in Example 1B. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 2B. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例3B>
活性炭の準備
比較例3Aで得た活性炭を準備した。
<Comparative Example 3B>
Preparation of activated carbon The activated carbon obtained in Comparative Example 3A was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Bで準備した薬剤溶液Bに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例3Bの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution B prepared in Example 1B. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 3B. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例4B>
活性炭の準備
有機質材料として、軟化点が280℃の粒状石炭ピッチ100質量部に対してトリスアセチルアセトナトイットリウム1.3質量部を混合したものを、溶融押出機に供給し、溶融温度320℃で溶融混合し、吐出量20g/minで紡糸することによりピッチ繊維を得た。得られたピッチ繊維を空気中常温から354℃まで1〜30℃/分の割合で54分間昇温することにより不融化処理をおこない、不融化されたピッチ繊維である活性炭前駆体を得た。得られた活性炭前駆体を、H2O濃度が100容量%のガスを賦活炉内に連続的に導入し、雰囲気温度900℃で25分間熱処理することにより賦活をおこない、繊維状活性炭を得た。得られた繊維状活性炭の0.65nm以上2.0nm以下の細孔径の細孔容積は0.337cc/gであった。また、全細孔容積は1.039cc/g、2nm以下の細孔径の細孔容積は0.395cc/g、比表面積は1248m2/g、0.65nm以下の細孔径の細孔容積は0.059cc/g、2nm以上3nm以下の細孔径の細孔容積は0.194cc/g、3nm以上の細孔径の細孔容積は0.450cc/gであった。
<Comparative Example 4B>
Preparation of activated carbon As an organic material, a mixture of 1.3 parts by mass of trisacetylacetonatoyttrium with 100 parts by mass of granular coal pitch with a softening point of 280 ° C. is supplied to a melt extruder at a melting temperature of 320 ° C. Pitch fibers were obtained by melt mixing and spinning at a discharge rate of 20 g / min. The pitch fiber thus obtained was heated in the air at a rate of 1 to 30 ° C./min for 54 minutes from room temperature to 354 ° C. to obtain an activated carbon precursor which was an infusible pitch fiber. The obtained activated carbon precursor was activated by continuously introducing a gas having an H 2 O concentration of 100% by volume into an activation furnace and heat-treating it at an ambient temperature of 900 ° C. for 25 minutes to obtain a fibrous activated carbon. . The resulting fibrous activated carbon had a pore volume of a pore diameter of 0.65 nm to 2.0 nm of 0.337 cc / g. The total pore volume is 1.039 cc / g, the pore volume of 2 nm or less is 0.395 cc / g, the specific surface area is 1248 m 2 / g, and the pore volume of 0.65 nm or less is 0. The pore volume of pore diameters of 0.059 cc / g, 2 nm or more and 3 nm or less was 0.194 cc / g, and the pore volume of pore diameters of 3 nm or more was 0.450 cc / g.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Bで準備した薬剤溶液Bに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例4Bの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution B prepared in Example 1B. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 4B. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of activated carbon ( Mass part) was measured in the same manner as in Example 1A.

実施例1B、実施例2B、比較例1B〜4Bで得た脱臭材を用い、比表面積、アセトアルデヒド平衡吸着量を前述の方法に従い、測定した。また、得られた脱臭材の比表面積から活性炭の比表面積を減じ、芳香族アミン及び硫酸の担持により減少した比表面積を算出した。また、上記アセトアルデヒド平衡吸着量は、比較例2Aの平衡吸着量を1としたときの比で評価した。結果を表2に示す。   Using the deodorizing materials obtained in Example 1B, Example 2B, and Comparative Examples 1B to 4B, the specific surface area and the acetaldehyde equilibrium adsorption amount were measured according to the methods described above. Further, the specific surface area of the activated carbon was subtracted from the specific surface area of the obtained deodorizing material, and the specific surface area decreased due to the loading of the aromatic amine and sulfuric acid was calculated. Moreover, the said acetaldehyde equilibrium adsorption amount was evaluated by the ratio when the equilibrium adsorption amount of Comparative Example 2A was 1. The results are shown in Table 2.

Figure 0006471256
Figure 0006471256

<試験例Bの小括>
実施例1B及び2Bは、活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、前記活性炭が、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上であることから、同じ浸漬条件で芳香族アミノ酸と硫酸を、上記活性炭以外の活性炭、すなわち、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g未満の比較例1B〜4Bの活性炭、に担持させた場合に比して、優れたアセトアルデヒド吸着性能を発揮するものであった。
<Summary of Test Example B>
Examples 1B and 2B include activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine supported on the activated carbon, or (B) an aromatic amine, a sulfate of the aromatic amine, and A deodorizing material containing sulfuric acid, wherein the activated carbon has a pore volume of 0.6 cc / g or more and a pore size of 0.6 cc / g or more. Compared to the case where sulfuric acid is supported on activated carbon other than the above activated carbon, that is, activated carbons of Comparative Examples 1B to 4B having a pore volume of 0.65 nm or more and 2.0 nm or less and a pore volume of less than 0.6 cc / g. In addition, it exhibited excellent acetaldehyde adsorption performance.

[試験例C]
<実施例1C>
活性炭の準備
実施例1Aで得た活性炭を準備した。
[Test Example C]
<Example 1C>
Preparation of activated carbon The activated carbon obtained in Example 1A was prepared.

本発明の脱臭材に含まれる薬剤溶液Cの調製
まず、75質量%の濃度で硫酸を含有した硫酸水溶液を調製した。この硫酸水溶液を65℃以上の温度で撹拌して、芳香族アミンとしてp−アミノ安息香酸を水溶液に加え、完全に溶解させたのち、活性炭の質量と処理液の体積との比が20g/Lとなるように水を加え、処理液を得た。なお、芳香族アミン及び硫酸の仕込み量は、活性炭100質量部に対して30.0質量部となるようにした。なお、硫酸の当該仕込み量(質量部)は、75硫酸水溶液中の、純水を除いた硫酸のみの量(質量部)を示す。
Preparation of drug solution C contained in deodorizing material of the present invention First, a sulfuric acid aqueous solution containing sulfuric acid at a concentration of 75% by mass was prepared. After stirring this sulfuric acid aqueous solution at a temperature of 65 ° C. or more and adding p-aminobenzoic acid as an aromatic amine to the aqueous solution and completely dissolving it, the ratio of the mass of activated carbon to the volume of the treatment liquid is 20 g / L. Water was added to obtain a treatment solution. The amount of aromatic amine and sulfuric acid charged was 30.0 parts by mass with respect to 100 parts by mass of activated carbon. In addition, the said preparation amount (mass part) of a sulfuric acid shows the quantity (mass part) of only the sulfuric acid except a pure water in 75 sulfuric acid aqueous solution.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、薬剤溶液Cに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、実施例1Cの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution C. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain the deodorizing material of Example 1C. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<実施例2C>
活性炭の準備
実施例2Bで得た活性炭を準備した。
<Example 2C>
Preparation of activated carbon The activated carbon obtained in Example 2B was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Cで準備した薬剤溶液Cに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、実施例2Cの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution C prepared in Example 1C. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain the deodorizing material of Example 2C. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例1C>
活性炭の準備
比較例1Aで得た活性炭を準備した。
<Comparative Example 1C>
Preparation of activated carbon The activated carbon obtained in Comparative Example 1A was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Cで準備した薬剤溶液Cに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例1Bの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution C prepared in Example 1C. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 1B. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例2C>
活性炭の準備
比較例2Aで得た活性炭を準備した。
<Comparative Example 2C>
Preparation of activated carbon The activated carbon obtained in Comparative Example 2A was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Cで準備した薬剤溶液Cに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例2Cの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution C prepared in Example 1C. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 2C. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例3C>
活性炭の準備
比較例3Aで得た活性炭を準備した。
<Comparative Example 3C>
Preparation of activated carbon The activated carbon obtained in Comparative Example 3A was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Cで準備した薬剤溶液Cに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例3Cの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution C prepared in Example 1C. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 3C. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

<比較例4C>
活性炭の準備
比較例4Bで得た活性炭を準備した。
<Comparative Example 4C>
Preparation of activated carbon The activated carbon obtained in Comparative Example 4B was prepared.

活性炭への本発明の脱臭材に含まれる薬剤の担持
次に、実施例1Cで準備した薬剤溶液Cに、上記得られた活性炭100質量部を浸漬した。続いて、この溶液を10分間に亘って撹拌して、活性炭を溶液中に均一に分散させた。その後、この分散液を静置した。8時間以上静置した後、活性炭を溶液から引き上げ、乾燥機を用いて80℃で3時間に亘って乾燥させ、比較例4Cの脱臭材を得た。なお、脱臭材における、活性炭100質量部に対する芳香族アミンと該芳香族アミンの硫酸塩の合計担持量(質量部)、及び活性炭100質量部に対する芳香族アミンの硫酸塩と硫酸の合計担持量(質量部)は、実施例1Aと同様に測定した。
Loading of the drug contained in the deodorizing material of the present invention on activated carbon Next, 100 parts by mass of the obtained activated carbon was immersed in the drug solution C prepared in Example 1C. Subsequently, the solution was stirred for 10 minutes to disperse the activated carbon uniformly in the solution. Thereafter, this dispersion was allowed to stand. After leaving still for 8 hours or more, the activated carbon was pulled up from the solution and dried at 80 ° C. for 3 hours using a dryer to obtain a deodorizing material of Comparative Example 4C. In addition, in the deodorizing material, the total supported amount (mass part) of the aromatic amine and sulfate of the aromatic amine with respect to 100 parts by mass of the activated carbon, and the total supported amount of sulfate and sulfuric acid of the aromatic amine with respect to 100 parts by mass of the activated carbon ( Mass part) was measured in the same manner as in Example 1A.

実施例1C、実施例2C、比較例1C〜4Cで得た脱臭材を用い、比表面積、アセトアルデヒド平衡吸着量を前述の方法に従い、測定した。また、得られた脱臭材の比表面積から活性炭の比表面積を減じ、芳香族アミン及び硫酸の担持により減少した比表面積を算出した。また、上記アセトアルデヒド平衡吸着量は、比較例2Aの平衡吸着量を1としたときの比で評価した。結果を表3に示す。   Using the deodorizing materials obtained in Example 1C, Example 2C, and Comparative Examples 1C to 4C, the specific surface area and the acetaldehyde equilibrium adsorption amount were measured according to the methods described above. Further, the specific surface area of the activated carbon was subtracted from the specific surface area of the obtained deodorizing material, and the specific surface area decreased due to the loading of the aromatic amine and sulfuric acid was calculated. Moreover, the said acetaldehyde equilibrium adsorption amount was evaluated by the ratio when the equilibrium adsorption amount of Comparative Example 2A was 1. The results are shown in Table 3.

Figure 0006471256
Figure 0006471256

<試験例Cの小括>
実施例1C及び2Cは、活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、前記活性炭が、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上であることから、同じ浸漬条件で芳香族アミノ酸と硫酸を、上記活性炭以外の活性炭、すなわち、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g未満の比較例1C〜4Cの活性炭、に担持させた場合に比して、優れたアセトアルデヒド吸着性能を発揮するものであった。
<Summary of Test Example C>
Examples 1C and 2C include activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine supported on the activated carbon, or (B) an aromatic amine, a sulfate of the aromatic amine, and A deodorizing material containing sulfuric acid, wherein the activated carbon has a pore volume of 0.6 cc / g or more and a pore size of 0.6 cc / g or more. Compared to the case where sulfuric acid is supported on activated carbon other than the above activated carbon, that is, activated carbons of Comparative Examples 1C to 4C having a pore volume of 0.65 nm or more and 2.0 nm or less and a pore volume of less than 0.6 cc / g. In addition, it exhibited excellent acetaldehyde adsorption performance.

また、試験例Cにおける実施例1C及び2Cについて、薬剤担持前の活性炭と担持後の脱臭材の、細孔分布を測定した。測定した細孔分布について、表4及び表5に示す。   For Examples 1C and 2C in Test Example C, the pore distributions of the activated carbon before loading the drug and the deodorizing material after loading were measured. Table 4 and Table 5 show the measured pore distribution.

Figure 0006471256
Figure 0006471256

Figure 0006471256
Figure 0006471256

表4及び表5から、0.65〜2.0nmの範囲の細孔容積の減少率が高かったことが明らかとなった。このことは、あらゆる細孔径の中でも、当該範囲の細孔径の細孔内に上記薬剤がより多く担持されることを示すと考えられる。   From Table 4 and Table 5, it became clear that the decreasing rate of the pore volume in the range of 0.65 to 2.0 nm was high. This is considered to indicate that a larger amount of the drug is supported in pores having a pore diameter in the above range among all pore diameters.

[試験例D]
(実施例1D(脱臭シートの製造))
実施例2Bで得た脱臭材と、バインダー繊維(ユニチカ株式会社製商品名メルティ4080)とを、質量比(バインダー/脱臭材)が25/75となるように混綿し、カーディング法により不織布ウエブを形成した。得られた不織布ウエブを所定枚数積層し、ニードルパンチングにより繊維を交絡させたのち、温度110℃で加熱してバインダー繊維を溶融させ、バインダー繊維と脱臭材とを融着させて、厚さ0.65mm、密度0.12g/cm3の脱臭シートを得た。なお、該脱臭シート中の脱臭材の目付は、56g/m2であった。
[Test Example D]
(Example 1D (production of deodorizing sheet))
The deodorizing material obtained in Example 2B and the binder fiber (trade name Melty 4080, manufactured by Unitika Ltd.) were mixed so that the mass ratio (binder / deodorizing material) was 25/75, and the nonwoven fabric web was formed by the carding method. Formed. A predetermined number of the obtained non-woven webs were laminated, and the fibers were entangled by needle punching, then heated at a temperature of 110 ° C. to melt the binder fibers, and the binder fibers and the deodorizing material were fused to obtain a thickness of 0. A deodorizing sheet having a density of 65 mm and a density of 0.12 g / cm 3 was obtained. The basis weight of the deodorizing material in the deodorizing sheet was 56 g / m 2 .

(実施例2D)
実施例2Cで得た脱臭材と、バインダー繊維(ユニチカ株式会社製商品名メルティ4080)とを、質量比(バインダー/脱臭材)が25/75となるように混綿し、カーディング法により不織布ウエブを形成した。得られた不織布ウエブを所定枚数積層し、ニードルパンチングにより繊維を交絡させたのち、温度110℃で加熱してバインダー繊維を溶融させ、バインダー繊維と脱臭材とを融着させて、厚さ0.65mm、密度0.12g/cm3の脱臭シートを得た。なお、該脱臭シート中の脱臭材の目付は、56g/m2であった。
(Example 2D)
The deodorizing material obtained in Example 2C and the binder fiber (trade name Melty 4080, manufactured by Unitika Ltd.) were mixed so that the mass ratio (binder / deodorizing material) was 25/75, and the nonwoven fabric web was formed by the carding method. Formed. A predetermined number of the obtained non-woven webs were laminated, and the fibers were entangled by needle punching, then heated at a temperature of 110 ° C. to melt the binder fibers, and the binder fibers and the deodorizing material were fused to obtain a thickness of 0. A deodorizing sheet having a density of 65 mm and a density of 0.12 g / cm 3 was obtained. The basis weight of the deodorizing material in the deodorizing sheet was 56 g / m 2 .

(実施例3D)
実施例2Cで得た脱臭材と、バインダー繊維(ユニチカ株式会社製商品名メルティ4080)とを、質量比(バインダー/脱臭材)が72/28となるように混綿し、カーディング法により不織布ウエブを形成した。得られた不織布ウエブを所定枚数積層し、ニードルパンチングにより繊維を交絡させたのち、温度110℃で加熱してバインダー繊維を溶融させ、バインダー繊維と脱臭材とを融着させて、厚さ0.35mm、密度0.14g/cm3の脱臭シートを得た。なお、該脱臭シート中の脱臭材の目付は、14g/m2であった。
(Example 3D)
The deodorizing material obtained in Example 2C and the binder fiber (trade name Melty 4080, manufactured by Unitika Ltd.) were mixed so that the mass ratio (binder / deodorizing material) was 72/28, and the nonwoven fabric web was formed by the carding method. Formed. A predetermined number of the obtained non-woven webs were laminated, and the fibers were entangled by needle punching, then heated at a temperature of 110 ° C. to melt the binder fibers, and the binder fibers and the deodorizing material were fused to obtain a thickness of 0. A deodorizing sheet having a density of 35 mm and a density of 0.14 g / cm 3 was obtained. The basis weight of the deodorizing material in the deodorizing sheet was 14 g / m 2 .

(脱臭シートの性能評価)
得られた脱臭シートの任意重量の試料片と100ppmアセトアルデヒドガス3Lを密閉容器に封入し、40℃の環境下において静置した。24時間経過後、容器内のガス濃度を測定し、吸着量を計算した。複数の試料重量について測定を行い、それぞれの計算結果より、濃度と吸着量の相関をグラフにプロットし、得られた関係式より、任意の平衡濃度におけるアセトアルデヒドの平衡吸着量(mg/gACF)を導いた。アセトアルデヒドの濃度測定は、ガスクロマトグラフィーによりおこなった。
(Performance evaluation of deodorizing sheet)
A sample piece of an arbitrary weight of the obtained deodorizing sheet and 3 L of 100 ppm acetaldehyde gas were sealed in a sealed container and allowed to stand in an environment of 40 ° C. After 24 hours, the gas concentration in the container was measured and the adsorption amount was calculated. Measure the weight of multiple samples, plot the correlation between concentration and adsorption amount on the graph from each calculation result, and calculate the equilibrium adsorption amount (mg / g ACF) of acetaldehyde at any equilibrium concentration from the obtained relational expression. lead. The concentration of acetaldehyde was measured by gas chromatography.

実施例1D〜3Dの結果を表6に示す。   The results of Examples 1D to 3D are shown in Table 6.

Figure 0006471256
Figure 0006471256

表6に示されるように、実施例1D〜3Dの脱臭シートは、本発明の脱臭材を含むものであることから、アセトアルデヒド吸着性能を効率良く発揮させるものであった。   As shown in Table 6, the deodorizing sheets of Examples 1D to 3D included the deodorizing material of the present invention, and thus exhibited the acetaldehyde adsorption performance efficiently.

Claims (9)

活性炭と、前記活性炭に担持された、(A)芳香族アミン及び該芳香族アミンの硫酸塩、又は、(B)芳香族アミン、該芳香族アミンの硫酸塩、及び硫酸とを含む、脱臭材であって、
前記(A)又は(B)を担持する前の活性炭は、全細孔容積が0.7〜2.0cc/gであり、
前記(A)又は(B)を担持する前の活性炭は、0.65nm以上2.0nm以下の細孔径の細孔容積が0.6cc/g以上であり、
前記(A)又は(B)を担持する前の活性炭は、全細孔容積に対する0.65nm以上2.0nm以下の細孔径の細孔容積の割合が0.6〜0.9であり、
前記(A)又は(B)を担持する前の活性炭は、0.65nm以下の細孔径の細孔容積が0.05〜0.12cc/gである、アセトアルデヒド又はホルムアルデヒドの脱臭材。
A deodorizing material comprising activated carbon and (A) an aromatic amine and a sulfate of the aromatic amine, or (B) an aromatic amine, a sulfate of the aromatic amine, and sulfuric acid supported on the activated carbon. Because
The activated carbon before supporting (A) or (B) has a total pore volume of 0.7 to 2.0 cc / g,
Activated carbon before carrying said (A) or (B) state, and are more than 2.0nm or less of the pore volume of pore diameters 0.6 cc / g or more 0.65 nm,
The activated carbon before supporting the (A) or (B) has a pore volume ratio of 0.6 to 0.9 to 0.6 to 0.9 nm with respect to the total pore volume,
Wherein (A) or (B) activated carbon before carrying is, 0.65 nm Ru pore volume 0.05~0.12cc / g der the following pore diameters, acetaldehyde or deodorant formaldehyde.
前記芳香族アミン及び該芳香族アミンの硫酸塩の合計担持量が、前記(A)又は(B)を担持する前の活性炭100質量部に対し、25〜35質量部であり、かつ、前記芳香族アミンの硫酸塩及び硫酸の合計担持量が、前記(A)又は(B)を担持する前の活性炭100質量部に対し、2〜5質量部である、請求項1に記載の脱臭材。The total carrying amount of the aromatic amine and sulfate of the aromatic amine is 25 to 35 parts by mass with respect to 100 parts by mass of the activated carbon before carrying the (A) or (B), and the fragrance The deodorizing material according to claim 1, wherein the total supported amount of the sulfate and sulfuric acid of the group amine is 2 to 5 parts by mass with respect to 100 parts by mass of the activated carbon before supporting (A) or (B). 前記(A)又は(B)を担持する前の活性炭は、全細孔容積(cc/g)が前記0.65nm以上2.0nm以下の細孔径の細孔容積の1〜2倍である、請求項1又は2に記載の脱臭材。 The activated carbon before supporting ( A) or (B) has a total pore volume (cc / g) of 1 to 2 times the pore volume of the pore diameter of 0.65 nm to 2.0 nm, The deodorizing material according to claim 1 or 2 . 前記(A)又は(B)を担持する前の活性炭の3nm以上の細孔径の細孔容積が0.02cc/g以下である、請求項1〜3のいずれかに記載の脱臭材。 The deodorizing material according to any one of claims 1 to 3 , wherein a pore volume having a pore diameter of 3 nm or more of the activated carbon before supporting the ( A) or (B) is 0.02 cc / g or less. 前記(A)又は(B)を担持する前の活性炭の比表面積が1500m2/g以上である、請求項1〜のいずれか1項に記載の脱臭材。 The deodorizing material according to any one of claims 1 to 4 , wherein a specific surface area of the activated carbon before supporting the ( A) or (B) is 1500 m 2 / g or more. 前記脱臭材の比表面積が400〜1200m2/gである、請求項1〜のいずれか1項に記載の脱臭材。 The deodorizing material according to any one of claims 1 to 5 , wherein the deodorizing material has a specific surface area of 400 to 1200 m 2 / g. 前記(A)又は(B)を担持する前の活性炭の比表面積から前記脱臭材の比表面積を減じた値が800〜1300m2/gである、請求項1〜のいずれか1項に記載の脱臭材。 The value which reduced the specific surface area of the said deodorizing material from the specific surface area of the activated carbon before carrying said ( A) or (B) is 800-1300m < 2 > / g, It is any one of Claims 1-6. Deodorizing material. 平衡濃度10ppmにおけるアセトアルデヒドの平衡吸着量(mg/gACF)が35mg/gACF以上である、請求項1〜のいずれか1項に記載の脱臭材。 The deodorizing material according to any one of claims 1 to 7 , wherein an equilibrium adsorption amount (mg / g ACF) of acetaldehyde at an equilibrium concentration of 10 ppm is 35 mg / g ACF or more. 請求項1〜のいずれか1項に記載の脱臭材を含む、アセトアルデヒド又はホルムアルデヒドの脱臭シート。 A deodorizing sheet of acetaldehyde or formaldehyde containing the deodorizing material according to any one of claims 1 to 8 .
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