JPS59186641A - Adsorbent for filter for cleaning atmospheric air - Google Patents

Adsorbent for filter for cleaning atmospheric air

Info

Publication number
JPS59186641A
JPS59186641A JP58060486A JP6048683A JPS59186641A JP S59186641 A JPS59186641 A JP S59186641A JP 58060486 A JP58060486 A JP 58060486A JP 6048683 A JP6048683 A JP 6048683A JP S59186641 A JPS59186641 A JP S59186641A
Authority
JP
Japan
Prior art keywords
activated carbon
adsorbent
filter
pore volume
pore diameter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP58060486A
Other languages
Japanese (ja)
Other versions
JPS6251651B2 (en
Inventor
Nobuo Ishizaki
石崎 信男
Hiroshi Shimizu
博 清水
Kenji Saida
斉田 健治
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyobo Co Ltd
Original Assignee
Toyobo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP58060486A priority Critical patent/JPS59186641A/en
Publication of JPS59186641A publication Critical patent/JPS59186641A/en
Publication of JPS6251651B2 publication Critical patent/JPS6251651B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3242Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
    • B01J20/3268Macromolecular compounds
    • B01J20/3272Polymers obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To improve adsorptive performance of active carbon for harmful gases in the atmospheric air by depositing additionally polyalkyleneimine to the active carbon. CONSTITUTION:0.1-50wt% polyalkyleneimine such as polyethyleneimine having 300-100,000 average mol.wt. is deposited to active carbon having >=0.15cc/g pore volume for 30-300Angstrom pore size. For the deposition of polyalkyleneimine, a soln. of polyalkyleneimine is applied by spraying and then drying, or by other process.

Description

【発明の詳細な説明】 本発明は、大気中の有害ガスに対して優れた吸着性能を
有する活性炭素吸着剤に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an activated carbon adsorbent having excellent adsorption performance for harmful gases in the atmosphere.

一般に、活性炭素吸着剤は、大気中の悪臭物質を低濃度
でも比較的高い平衡吸着量で吸着するため、他の吸着剤
に比較して有利であり1現在広く利用されている。しか
し、ホルムアルデヒド、アセトアルデヒド?アクロレイ
ンtシアン、硫化水素、メルカプタン−の如き低濃度で
刺激性の強いガス成分に対しては平衡吸着量が低く、か
つ吸着したガスが濃縮されて脱着するという欠点を有し
ていた。
In general, activated carbon adsorbents adsorb malodorous substances in the atmosphere with a relatively high equilibrium adsorption amount even at low concentrations, and are therefore advantageous compared to other adsorbents and are currently widely used. But formaldehyde, acetaldehyde? It has the disadvantage that the equilibrium adsorption amount is low for gas components that are highly irritating at low concentrations such as acrolein cyanide, hydrogen sulfide, and mercaptan, and that the adsorbed gas is concentrated and then desorbed.

上記欠点を解消すべく、塩化アンモニウムの如きアンモ
ニウム塩を通常の粒状活性炭に添着してアルデヒド類を
除大方法(特開昭53−29292号)あるいは、エチ
レンジアミン、トリエチレンテトラミン、アニソン等の
低分子アミン類を添着してアルデヒド類を除去する方法
(特開昭56−53744号)が提案されている。しが
しながら従来の添着用活性炭はヤシガラ系あるいは石炭
系の活性炭であるため、細孔直径30〜300X(7)
細孔容積量が小さいため添着剤の添着効果が小さいとい
う欠点を有しせり。さらに、従来の添着剤は低分子であ
るため、添着担体である活性炭のミクロな細孔を閉塞し
やすいため、吸着性能の改良効果が小さいこと、又使用
時の再飛散の問題があった。
In order to solve the above drawbacks, a method for removing aldehydes by impregnating ordinary granular activated carbon with an ammonium salt such as ammonium chloride (Japanese Unexamined Patent Publication No. 53-29292), or a method using low molecular weight compounds such as ethylenediamine, triethylenetetramine, and anison, etc. A method has been proposed in which aldehydes are removed by impregnating amines (Japanese Patent Application Laid-Open No. 56-53744). However, since conventional activated carbon for impregnation is coconut shell-based or coal-based activated carbon, the pore diameter is 30 to 300X (7).
Since the pore volume is small, the impregnating effect of the adhesive is small. Furthermore, since conventional impregnants have low molecular weight, they tend to clog the microscopic pores of activated carbon, which is the impregnating carrier, so that the effect of improving adsorption performance is small and there is a problem of re-scattering during use.

本発明は、かかる欠点を解消すべく鋭意・検別の結果、
見い出されたものである。即ち1細孔直径30〜30o
Xの細孔容積がo、1acc/9以上の活性炭素材にポ
リアルキレンイミンを添着させた大気浄化フィルター用
吸着剤を見い出したものである。
The present invention has been made as a result of careful examination to eliminate such drawbacks.
This is what was discovered. That is, 1 pore diameter 30~30o
An adsorbent for air purification filters has been discovered in which a polyalkylene imine is impregnated with an activated carbon material having a pore volume of X of o, 1 acc/9 or more.

本発明に用いられる活性炭素材は細孔直径30λ〜30
0λの細孔の容積が0.15eC/9以上の活性炭素材
であることがシアン系、アルデヒド類。
The activated carbon material used in the present invention has a pore diameter of 30λ to 30
Cyanide and aldehydes are activated carbon materials with a pore volume of 0λ of 0.15eC/9 or more.

硫化水素、メルカプタン類等の刺激性有害ガスを効率よ
く除去する点で必要である0即ち、細孔直径30X 〜
3002の細孔容積が0.15eC/G1未満の活性炭
素(り使用では、本発明で用いるポリアルキレンイミン
、例えばエチレンイミン重合体を添着したとしてもその
添着効果が充分でなく、本発明のような効果が充分に発
揮しえないので好ましくない。また細孔直径が30A未
満の細孔ではアルキレンイミン重合体が添着されても平
面的な表面しか形成せず、また細孔径が30OAをこえ
ると表面積が著しく低下するので好ましくない。
0, that is, pore diameter 30X, which is necessary for efficiently removing irritating and harmful gases such as hydrogen sulfide and mercaptans.
3002 with a pore volume of less than 0.15eC/G1, the impregnation effect is not sufficient even if the polyalkyleneimine used in the present invention, for example, ethyleneimine polymer, is impregnated. This is not preferable because the effect cannot be fully exhibited.Also, in pores with a pore diameter of less than 30A, only a flat surface will be formed even if the alkyleneimine polymer is impregnated, and if the pore diameter exceeds 30OA, This is not preferred because the surface area is significantly reduced.

尚、活性炭素の細孔直径および細孔容積は、常圧下の液
体窒素の沸点(−195,8℃)における吸着側の窒素
ガス吸着等混線を用いてクランストン−インクレー(O
ra:e+5ton−工nkley )の計算法により
求めた。なお、多分子吸着層と相対圧との関係はt (
A ): 4.3 (5/In (Pa/P)) V”
なるフレンケルーハンシ−(Frenkel −Hal
sey )の式(慶伊富長「吸着」共立出版)より計算
した。
The pore diameter and pore volume of activated carbon are calculated using Cranston-Inklay (O
ra: e+5ton-enginekley). The relationship between the multimolecular adsorption layer and the relative pressure is t (
A): 4.3 (5/In (Pa/P)) V”
Frenkel-Hal
sey ) (Keii Tominaga "Adsorption" Kyoritsu Shuppan).

上記、特定の細孔径において大きり細孔の容積を有する
活性炭素材は例えば次のような方法で製造される。即ち
、(1)セルロース系繊維状活性炭に塩化第2鉄、酢酸
マグネシウム等の酸化触媒を担持後、高温の水蒸気ガス
雰囲気下で再活性化処理を施し作製される。さらに(1
1)木材バルブの微粉末等を炭化後、900〜1300
℃の高温水蒸気含有燃焼ガス雰囲気下で、高度に活性化
処理を施し作製される。あるいは(呻畜牛や水牛の骨を
蒸し焼きすることにより得られる骨炭(bone ch
ar )や血液を炭酸カリとともに熱分解して得られる
血炭のような動物性活性炭素(例えば、荒木鶴雄「活性
炭素」(丸@))、さらには0ψおがくず、水利パルプ
、再生セルロース繊維、木綿等を濃厚な塩化亜鉛、燐酸
、塩化力ルンウム等酸性水溶液Gこ混合し、600〜9
00℃で不活性雰囲気下焼成7、賦活する方法あるいは
(V)石油生コークス、カーボンブラック、オイルカー
ボン、アスファルト1活性炭等を水酸化カリウム、硫化
力1ノウム、炭酸カリウム、硫酸カリウム等の薬剤で7
00〜1200℃で加熱処理する方法で作製されるもの
等を挙げることができる。もちろん細孔直径が30〜3
00Aの細孔の容積が0.15cc/G’以上の活性炭
素を与える方法であれば上記方法に限定されるもので番
まない。
The above-mentioned activated carbon material having a large pore volume at a specific pore diameter is produced, for example, by the following method. That is, (1) it is produced by supporting an oxidation catalyst such as ferric chloride or magnesium acetate on cellulose-based fibrous activated carbon, and then subjecting it to reactivation treatment in a high-temperature steam gas atmosphere. Furthermore (1
1) After carbonizing fine wood valve powder, etc., 900 to 1300
It is manufactured through highly activated treatment in a combustion gas atmosphere containing high-temperature water vapor at ℃. Or (bone char obtained by steaming the bones of cattle or water buffalo)
ar) and animal activated carbon such as blood charcoal obtained by thermally decomposing blood with potassium carbonate (for example, Tsuruo Araki's "Activated Carbon" (Maru@)), as well as 0ψ sawdust, water pulp, regenerated cellulose fiber, Mix cotton, etc. with an acidic aqueous solution such as zinc chloride, phosphoric acid, or chloride, and add 600 to 9
Calcination in an inert atmosphere at 00°C 7, Activation method or (V) Petroleum raw coke, carbon black, oil carbon, asphalt 1 activated carbon, etc. with agents such as potassium hydroxide, sulfurizing power 1, potassium carbonate, potassium sulfate, etc. 7
Examples include those produced by a method of heat treatment at 00 to 1200°C. Of course, the pore diameter is 30-3
The method is not limited to the above method as long as it provides activated carbon with a 00A pore volume of 0.15 cc/G' or more.

一方本発明に用いるポリアルキレンイミン番まア例えば
エチレンイミンを適当な触媒で開環重合させて得られる
f OH,OH,NH’j nをくり返し単位とする平
均分子量が300〜100000のポリエチレンイミン
が用いられる。またポリアルキレンイミンの活性炭素材
への添着蓋は0.1〜50重量%1好ましくは1〜30
重量%である。添着法は1ポリアルキレンイミン溶液を
スプレー塗布後、乾燥する方法あるいは所定濃度のポリ
アルキレンイミン水溶液に、所定量の活性炭素材を浸漬
し為ポリアルキレンイミン分子を吸着させ、濾過するこ
と等により得られる。又、湿式法でのフィルター成形法
を容易にするため、ポリエチレンイミンを添着後、10
0℃以上で加熱することにより、活性炭素材の一000
H基のような表面官能基と化学結合を生成させてもよい
。又、該活性炭素材上で、アルキレンイミンを重合させ
ることにより、ポリアルキレンイミンを添着させてもよ
い。
On the other hand, the polyalkyleneimine used in the present invention is, for example, polyethyleneimine having an average molecular weight of 300 to 100,000 and having repeating units of fOH, OH, NH'jn obtained by ring-opening polymerization of ethyleneimine with a suitable catalyst. used. In addition, the amount of polyalkyleneimine attached to the activated carbon material is 0.1 to 50% by weight, preferably 1 to 30% by weight.
Weight%. The impregnation method can be obtained by spraying a polyalkylene imine solution and then drying it, or by immersing a predetermined amount of activated carbon material in a polyalkylene imine aqueous solution of a predetermined concentration to adsorb polyalkylene imine molecules, and filtering. . In addition, in order to facilitate the filter molding method using the wet method, after impregnating polyethyleneimine, 10
By heating above 0℃, activated carbon material can be heated to 1000%
Chemical bonds may be formed with surface functional groups such as H groups. Alternatively, polyalkylene imine may be attached by polymerizing alkylene imine on the activated carbon material.

本発明に用いる活性炭素材の形状は繊維状1平均粒径が
200メツシユ(74μm)以下ノ微粉大のマクロポア
量の大きい造粒物(粒状物)等が添着効果の点より好ま
しい。
The shape of the activated carbon material used in the present invention is preferably a granulated material (granular material) having a fibrous average particle diameter of 200 mesh (74 .mu.m) or less and a large amount of macropores in the size of a fine powder from the viewpoint of the adhesion effect.

以下余白 本発明の吸着剤を用いるフィルター形成手段としては−
(1)微粉末状の活性炭素にポリエチレンを添着後Nア
ルギン酸ソーダ、カルボキシメチルセルロースル水ガラ
ス〜シリカゾル1ポリスチレン溶液等の溶液に分散し、
紙、布、フオーム材、段ボールシート%ハニカム状フィ
ルター、多孔性の粒状物等に塗布−乾燥してつくる方法
、あるいは(II)化学的に結合されたポリアルキレン
イミン添着活性炭素材を木材パルプ、繊維状ポリビニル
アルコール等と湿式混合抄紙し、通気性シートを得てフ
ィルターとする方法あるいは(110上記シートを段ボ
ール・シートに加工後、ハニカム状に成形し、フィルタ
ーを得る方法0φ該活性炭素材を通気性のあるシート状
あるいはシート化、段加工後、ポリアルキレンイミン添
着処理を施す方法あるいは()該微粉末状活性炭素材を
水ガラス、ポリビニルアルコール、粘土、メチルセルロ
ース等のバインダー用いて細孔直径、が約1000λ以
上のいわゆるマクロ・ボア量の多い多孔性粒状物に成型
後、添着処理を施し、充填層フィルターとして用いる方
法等がある。特に、吸着剤のガスへの接触効率と通気性
のバランスが良好なハニカム状フィルター、あるいは通
算性の良好な7オーム材・フィルターが好ましい6 本発明の吸着剤は、中分子量以上のポリアルキレンイラ
ン分子が特定の細孔分布をもつ活性炭素に添着されてい
るため、シアン系、アルデヒド類、硫化水素、メルカプ
タン類の如き有害かつ高刺激性ガスへの吸着性能が大で
あること、添着薬品の再飛散が無いこと、又、細孔閉塞
作用が少ないため活性炭本来の吸着作用の低下が小さい
という特徴を有する。従ってシアン・ホルムアルデヒド
、アセトアルデヒド、硫化水素等が充満しやすい自動車
内、電車車輌内、喫茶店1映画館、パチンコ屋あるいは
、家庭の居間に本発明に係る吸着剤を使用したフィルタ
ーを設置すると効率よく上記有害ガスを除失し、通気抵
抗も低く、室内の暖冷房効果を低下させることが少ない
というメリットを有する。
Below are the margins for forming a filter using the adsorbent of the present invention:
(1) After impregnating polyethylene on fine powdered activated carbon, disperse it in a solution such as N sodium alginate, carboxymethyl cellulose, water glass, silica sol, 1 polystyrene solution,
(II) Chemically bonded polyalkylene imine-impregnated activated carbon material is applied to wood pulp, fibers, etc. A method of wet-mixing the activated carbon material with polyvinyl alcohol, etc. to obtain a breathable sheet and making it into a filter, or (110) A method of forming the above sheet into a corrugated cardboard sheet and forming it into a honeycomb shape to obtain a filter. A method of applying polyalkyleneimine impregnation treatment after forming into a sheet or sheeting or step processing, or () using the finely powdered activated carbon material with a binder such as water glass, polyvinyl alcohol, clay, methyl cellulose, etc. to form a material with a pore diameter of approximately There are methods such as molding into porous granules with a large macro-pore volume of 1000λ or more, applying an impregnation treatment, and using them as a packed bed filter.In particular, the adsorbent has a good balance between contact efficiency with gas and air permeability. A honeycomb-like filter or a 7-ohm material/filter with good compatibility is preferred.6 The adsorbent of the present invention has polyalkylene ylang molecules of medium molecular weight or higher attached to activated carbon with a specific pore distribution. , cyanide, aldehydes, hydrogen sulfide, mercaptans, and other harmful and highly irritating gases; no re-scattering of impregnated chemicals; Therefore, the present invention can be used in a car, a train car, a coffee shop, a movie theater, a pachinko parlor, or a home living room where cyanide/formaldehyde, acetaldehyde, hydrogen sulfide, etc. are likely to be filled. Installing a filter using an adsorbent has the advantage of efficiently removing the above-mentioned harmful gases, having low ventilation resistance, and less reducing indoor heating and cooling effects.

以下本発明の実施例を記載するが本発明はこれら実施例
に限定されるものでない。
Examples of the present invention will be described below, but the present invention is not limited to these Examples.

実施例 L 比較例 L BIT法比法面表面積30cl//P  で細孔直径3
0〜300Aの細孔容[o、oacC/9(7)再生セ
/l/ a−ス糸繊維状活性炭に、酢酸マグネシラA1
0重電%を含浸−担持させた後、900tlの水蒸気含
有燃焼ガス雰囲気で悪活性化処理を施し、細孔直径30
〜300Aの細孔の容積がo、4o cc/9 (D繊
維状活性炭を得た。
Example L Comparative example L BIT method surface area 30cl//P and pore diameter 3
Pore volume of 0 to 300 A [o, oacC/9 (7) regenerated ce/l/a-thread fibrous activated carbon, magnesila acetate A1
After impregnating and supporting 0% heavy electric charge, an adverse activation treatment was performed in a combustion gas atmosphere containing 900 tl of water vapor, and the pore diameter was 30 ml.
~300A pore volume was o, 4o cc/9 (D fibrous activated carbon was obtained.

上記活性炭素60部、p水度がS R30’に叩解され
たNBKPパルプ(針葉樹ブリーチンダクラフトパルプ
)40部及びポリビニルアルコール繊維7部の組成で、
ヤンキー型湿式抄紙機で活性炭素ヘー バー ヲ459
 / ’の目付で抄造した。ペーパー厚み0.20 M
の活性炭素紙を得た。次いで該炭素紙をコルゲート加工
機でピッチ巾3,1m、ピッチ高E、l−の片面段ボー
ル・シートに形成した。該片面段ボール・シートを、ポ
リエチレンイミン(日本触媒化学工業■5p−200+
分子量10000 )の6重量%メタノール溶液に1昼
夜浸漬後、p過、乾燥シてポリエチレンイミンを30重
量%添着した片段ボール・シートを得た。
With a composition of 60 parts of the above activated carbon, 40 parts of NBKP pulp (softwood bleached craft pulp) beaten to a pH of S R30', and 7 parts of polyvinyl alcohol fiber,
Activated carbon heaving machine 459 with Yankee type wet paper machine
The paper was made with a weight of / '. Paper thickness 0.20M
Activated carbon paper was obtained. The carbon paper was then formed into a single-sided corrugated cardboard sheet with a pitch width of 3.1 m and a pitch height of E and l- using a corrugating machine. The single-sided corrugated cardboard sheet was made of polyethyleneimine (Nippon Shokubai Chemical Industry ■5p-200+
After being immersed in a 6 wt % methanol solution with a molecular weight of 10,000 for one day and night, it was filtered and dried to obtain a single corrugated cardboard sheet impregnated with 30 wt % polyethyleneimine.

該段ボール・シートを層長50m5のハニカム・フィル
ターに切断加工後アセトアルデヒドlOppmおよびシ
アン10ppn含有空気通気速度+50e+w/36c
で流したところ、第1表のような結果が得られた。
After cutting the corrugated sheet into honeycomb filters with a layer length of 50 m5, the air aeration rate was +50e+w/36c containing lOppm of acetaldehyde and 10ppn of cyanide.
The results shown in Table 1 were obtained.

なお、比較例として、該段ボール・シートにエチレンジ
アミンを添着したものから成るハニカム・フィルターの
性能評価を試みた(比較例1)。
As a comparative example, an attempt was made to evaluate the performance of a honeycomb filter made of the corrugated cardboard sheet to which ethylenediamine was attached (Comparative Example 1).

比較例 2 実施例1の前駆体活性炭素繊維(細孔直径30〜300
Aの細孔容積: 0.08匡/9)を用いて、実施例1
と同じように抄紙1段ボール、ポリエチレンイミン添着
処理後、ハニカム・フィルターをつくりNアセトアルデ
ヒド、シアンの性能評価を試みた。第1表に結果を示す
Comparative Example 2 Precursor activated carbon fiber of Example 1 (pore diameter 30-300
Example 1 using the pore volume of A: 0.08 squares/9)
In the same way as above, we made a honeycomb filter using paperboard and polyethyleneimine impregnation, and attempted to evaluate the performance of N-acetaldehyde and cyanide. Table 1 shows the results.

実施例 2 木材バルブの微粉末を500 ’Oの不活性算囲気下で
炭化処理後、1300℃の燃焼ガス剪囲気下ζ数秒活性
化処理を施し、細孔直径30〜300Aの細孔の容積が
0.29CC/9  の活性炭素を得た。該活性炭をボ
ール・ミルで粉砕処理し1平均粒径20μ胃の粉末状活
性炭素を得た。該活性炭を5重量%のポリエチレンイミ
ン(日本触媒化学工業h 、 Sp−018)俗液に1
昼夜浸漬にすることにより、ポリエチレンイミンを20
重量%吸着させ、濾過、乾燥した。該活性炭15部をア
ルギン酸ソーダ水浴a l 0部に分散し、均一なペー
ストをつくった後1?を厚30−のウレタン・フオーム
・シート(ブリジストンタイヤ■:エバライト・スコツ
トフィルター、HR−30)を浸漬、脱水、乾燥し、活
性炭添着シートを得た。         シ実施例1
と同様に、アセトアルデヒドおよびヤアン含有ガスの除
去能を評価した。その結果を第1表に示す。
Example 2 Fine wood valve powder was carbonized under an inert atmosphere of 500'O, and then activated for several seconds under a combustion gas shearing atmosphere of 1300°C to reduce the volume of pores with a pore diameter of 30 to 300A. Activated carbon of 0.29 CC/9 was obtained. The activated carbon was pulverized in a ball mill to obtain powdered activated carbon with an average particle size of 20 μm. The activated carbon was added to 5% by weight of polyethyleneimine (Nippon Shokubai Kagaku Kogyo h, Sp-018) common solution.
By soaking day and night, polyethyleneimine is
It was adsorbed in weight percent, filtered and dried. After dispersing 15 parts of the activated carbon in a sodium alginate water bath and making a uniform paste, 1. A 30-thick urethane foam sheet (Bridgestone Tire ■: Everite Scott Filter, HR-30) was immersed, dehydrated, and dried to obtain an activated carbon-impregnated sheet. Example 1
Similarly, the ability to remove acetaldehyde and Yaan-containing gas was evaluated. The results are shown in Table 1.

比較例 & 市販ヤシガラ活性炭(細孔直径30〜300χの細孔容
積o、1occ/9、BIT法比法面表面積100 d
/り)を粗粉砕後、ボール・ミルで平均粒径2oμ屑に
微粉砕した。
Comparative Example & Commercial coconut shell activated carbon (pore diameter 30-300χ, pore volume o, 1occ/9, BIT ratio normal surface area 100 d
/ri) was coarsely pulverized, and then finely pulverized using a ball mill into particles having an average particle size of 2 μm.

該活性炭を実施例2と同様に添着処理ポリエチレンイミ
ン処理を施し、ウレタンフオームフィルターを得、ガス
除去能を評価した。その結果も第1表に併記した。
The activated carbon was impregnated with polyethyleneimine in the same manner as in Example 2 to obtain a urethane foam filter, and its gas removal ability was evaluated. The results are also listed in Table 1.

以下余白 実施例 3、比較例 4 針葉樹系木材の鋸屑を平炉で一昼夜500℃で炭化処理
を施した。
The following are blank spaces: Example 3, Comparative Example 4 Sawdust from coniferous wood was carbonized at 500°C for one day and night in an open hearth.

該炭化物を流動賦活炉で滞留時間10〜15秒、温度1
200〜1300℃、水蒸気10%含有雰囲気で賦活処
理を施し、比表面積110011’/9、細孔直径30
〜300Aの細孔容積0.21cc/りの活性炭を得た
The carbide was heated in a fluidized activation furnace for a residence time of 10 to 15 seconds and a temperature of 1.
Activation treatment was performed at 200 to 1300°C in an atmosphere containing 10% water vapor, with a specific surface area of 110011'/9 and a pore diameter of 30.
Activated carbon with a pore volume of ~300 A and a pore volume of 0.21 cc/liter was obtained.

該活性炭をボール・ミルで平均粒径20μ爾に微粉砕し
た。
The activated carbon was pulverized in a ball mill to an average particle size of 20 μm.

該活性炭を水ガラスを用いて造粒処理を施した後、塩酸
浴液に浸漬して〜水ガラス・バインダーを不溶化した。
The activated carbon was granulated using water glass and then immersed in a hydrochloric acid bath to insolubilize the water glass binder.

粒度35〜50メツシユの粒状吸着材が得られた。A granular adsorbent with a particle size of 35 to 50 mesh was obtained.

該粒状活性炭材にポリエチレンイミン(日本触媒化学工
業■、p−1000,平均分子前o、ooo )の水浴
液に一昼夜浸漬後\乾燥することにより、10重量%の
添着飯をもつ吸着剤を得た。
The granular activated carbon material was immersed in a water bath solution of polyethyleneimine (Nippon Shokubai Kagaku Kogyo ■, p-1000, average molecular weight: o, ooo) for a day and night, and then dried to obtain an adsorbent with 10% by weight of impregnated iron. Ta.

比較例として 市販石炭系活性炭(細孔直径30〜300λの細孔容積
o、oacc/り、BKT法比法面表面積800w19
  )をボールミルで、平均粒径20plIに微粉砕後
、実施例3と同じく、水ガラスで造粒後、不溶化処理を
直径1,6 emのガラス製カラムに充填し、25p戸
の硫化木葉を含んだ空気を流速Locm/1gθ0で流
したところ、前者の初期除去率は100%であったのに
対し、後者の除去率は50%であった。
As a comparative example, commercially available coal-based activated carbon (pore diameter 30 to 300λ, pore volume o, oacc/r, BKT ratio slope surface area 800w19
) was pulverized with a ball mill to an average particle size of 20 plI, granulated with water glass as in Example 3, and then insolubilized into a glass column with a diameter of 1.6 em, containing 25 p of sulfurized tree leaves. When air was flowed at a flow rate of Locm/1gθ0, the initial removal rate of the former was 100%, while the removal rate of the latter was 50%.

実施例 4、比較例 6 牛骨を乾燥後16〜30メツシユに微粉砕し、石英管状
炉で窒素ガス気流下800’l:lまで約5時間で昇温
することにより、収率5o%でEFT法比表面積工00
ビ/y炭素含有量10 wt%の骨炭を得た。
Example 4, Comparative Example 6 After drying, beef bones were pulverized into 16 to 30 meshes and heated in a quartz tube furnace under a nitrogen gas stream to 800'l:l in about 5 hours, with a yield of 5o%. EFT method specific surface area processing 00
Bone charcoal with a bi/y carbon content of 10 wt% was obtained.

細孔直径30〜300χ細孔容積は0.18cc/pで
あった。
The pore diameter was 30 to 300χ and the pore volume was 0.18 cc/p.

いて造粒処理を施した後、塩酸浴液に浸漬して、水ガラ
ス・バインダーを不溶化した。
After granulation treatment was carried out using the same method, it was immersed in a hydrochloric acid bath solution to insolubilize the water glass binder.

粒度35〜5oメツシユの粒状吸着剤を得た。A granular adsorbent having a particle size of 35 to 5o mesh was obtained.

該吸着剤にポリエチレンイミン(日本触媒化学工業@A
  5p−006:分子it 600 ) 水溶Mニ&
[後、乾燥することにより20重量%の添着処理を施し
た。比較例として、市販パーム炭素活性炭(細孔直径3
0−300+Xの細孔容積o、obcc/g、EFT法
比表面積voo*/9)をボール・ミルで微粉砕後、水
ガラスで造粒後N不溶化処理をFifj L 、粒度3
δン(5p−006)を20重量%添着処理を施した。
The adsorbent contains polyethyleneimine (Nippon Shokubai Chemical Industry @A
5p-006: Molecule it 600) Water-soluble Mni&
[Then, a 20% by weight impregnation treatment was performed by drying. As a comparative example, commercially available palm carbon activated carbon (pore diameter 3
0-300+X pore volume o, obcc/g, EFT method specific surface area voo*/9) was finely pulverized in a ball mill, granulated with water glass, and then N insolubilized to Fifj L, particle size 3
An impregnation treatment of 20% by weight of δ-n (5p-006) was performed.

該吸着剤を一層高が3傷になるよう直径1.6(のガラ
ス製カラムに充填し、l Oppzのホルムアルデヒド
を含有した空気3流速10 cm / Becで流した
ところ、前者の初期除去率内95%であったのに対し・
後者の除去率は10%であった。
When the adsorbent was packed in a glass column with a diameter of 1.6 mm so that the height was 3 scratches, and air containing 1 Oppz of formaldehyde was flowed at a flow rate of 10 cm/Bec, the initial removal rate was within the former's initial removal rate. Whereas it was 95%.
The removal rate of the latter was 10%.

Claims (1)

【特許請求の範囲】 (1)細孔直径30〜300Aの細孔容積が0.158
f1!79以上の活性炭素材にポリアルキレンイミンを
添着させることを特徴とする大気浄化フィルター用吸着
剤。 (2)活性炭素材が、粉末状活性炭である特許請求の範
囲第(1)項記載の大気浄化フィルター用吸着剤。 (8)活性炭素材が繊維状活性炭である特許請求の範囲
第(1ン項記載の大気浄化フィルター用吸着剤。 (4)  ポリアルキレンイミンがポリエチレンイミン
である特許請求の範囲第(1)項記載の大気浄化フィル
ター用吸着剤。
[Claims] (1) Pore volume of pore diameter 30 to 300A is 0.158
An adsorbent for an air purification filter, characterized in that a polyalkylene imine is attached to an activated carbon material of f1!79 or more. (2) The adsorbent for an air purification filter according to claim (1), wherein the activated carbon material is powdered activated carbon. (8) The adsorbent for air purification filters according to claim 1, wherein the activated carbon material is fibrous activated carbon. (4) Claim 1, wherein the polyalkylene imine is polyethyleneimine. Adsorbent for air purification filters.
JP58060486A 1983-04-05 1983-04-05 Adsorbent for filter for cleaning atmospheric air Granted JPS59186641A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58060486A JPS59186641A (en) 1983-04-05 1983-04-05 Adsorbent for filter for cleaning atmospheric air

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58060486A JPS59186641A (en) 1983-04-05 1983-04-05 Adsorbent for filter for cleaning atmospheric air

Publications (2)

Publication Number Publication Date
JPS59186641A true JPS59186641A (en) 1984-10-23
JPS6251651B2 JPS6251651B2 (en) 1987-10-30

Family

ID=13143653

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58060486A Granted JPS59186641A (en) 1983-04-05 1983-04-05 Adsorbent for filter for cleaning atmospheric air

Country Status (1)

Country Link
JP (1) JPS59186641A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62216641A (en) * 1986-03-19 1987-09-24 Nippon Shokubai Kagaku Kogyo Co Ltd Adsorbent for purifying environment
JPS62231666A (en) * 1985-12-12 1987-10-12 馬場 照雄 Deodorizing material and its production
JP2003523468A (en) * 2000-01-26 2003-08-05 ビーエーエスエフ アクチェンゲゼルシャフト Modified polyurethane foam used as an adsorbent
KR100768406B1 (en) 2006-08-10 2007-10-18 한국원자력연구원 New innovative functional composites comprising mesoporous carbon-based material and functional polymer
JP2017213118A (en) * 2016-05-31 2017-12-07 住江織物株式会社 Deodorizing filter
CN113077994A (en) * 2021-02-24 2021-07-06 辽宁博艾格电子科技有限公司 Electrode plate for super capacitor and preparation method thereof

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62231666A (en) * 1985-12-12 1987-10-12 馬場 照雄 Deodorizing material and its production
JPH0622556B2 (en) * 1985-12-12 1994-03-30 照雄 馬場 Deodorizing material and manufacturing method thereof
JPS62216641A (en) * 1986-03-19 1987-09-24 Nippon Shokubai Kagaku Kogyo Co Ltd Adsorbent for purifying environment
JPH0417089B2 (en) * 1986-03-19 1992-03-25 Nippon Shokubai Kk
JP2003523468A (en) * 2000-01-26 2003-08-05 ビーエーエスエフ アクチェンゲゼルシャフト Modified polyurethane foam used as an adsorbent
JP4700250B2 (en) * 2000-01-26 2011-06-15 ビーエーエスエフ ソシエタス・ヨーロピア Modified polyurethane foam used as adsorbent
KR100768406B1 (en) 2006-08-10 2007-10-18 한국원자력연구원 New innovative functional composites comprising mesoporous carbon-based material and functional polymer
JP2017213118A (en) * 2016-05-31 2017-12-07 住江織物株式会社 Deodorizing filter
CN113077994A (en) * 2021-02-24 2021-07-06 辽宁博艾格电子科技有限公司 Electrode plate for super capacitor and preparation method thereof
CN113077994B (en) * 2021-02-24 2022-11-08 辽宁博艾格电子科技有限公司 Electrode plate for super capacitor and preparation method thereof

Also Published As

Publication number Publication date
JPS6251651B2 (en) 1987-10-30

Similar Documents

Publication Publication Date Title
US6156697A (en) Method of producing high surface area carbon structures
AU2017208389A1 (en) Desiccant based honeycomb chemical filter and method of manufacture thereof
KR101641985B1 (en) Honeycomb matrix comprising macroporous desiccant, process and use thereof
JPH08239279A (en) Nitrogen-containing molecular sieve activated carbon, production and use thereof
US6129846A (en) Activated carbon composite with crystalline tin silicate
JPH04200742A (en) Carbon dioxide adsorbent
JPWO2003022425A1 (en) Composite granular material and method for producing the same
JPS59186641A (en) Adsorbent for filter for cleaning atmospheric air
JP2015509832A (en) Desiccant-supporting honeycomb chemical filter and manufacturing method thereof
US3594982A (en) Process for drying unsaturated organic gaseous compounds
JPH0549918A (en) Carbon dioxide adsorbent
JP3540040B2 (en) Adsorbent manufacturing method
JPH08259344A (en) Porous adsorbing material
JPH01236941A (en) Gaseous ammonia adsorbent
JPS6044012B2 (en) Adsorbent for removing sulfur-containing harmful gases
JPH0280314A (en) Sheet containing active carbon
JPS59151882A (en) Selective adsorbent for tobacco filter
CN115087498A (en) Carbonaceous material, method for producing same, filter for water purification, and water purifier
JPH04503326A (en) Method for producing foam for absorbing organic substances
JPS6324413B2 (en)
CN207190459U (en) The base material with function of removing formaldehyde for automobile
JPS5950399A (en) Radioactive iodine removal filter
JP7290381B1 (en) Carbon dioxide adsorbent, carbon dioxide adsorption device, manufacturing method thereof, and carbon dioxide adsorption method.
JP2001239157A (en) Inorganic ion exchanger-hydrophilic polymer active carbon composite and its production method
RU2798457C1 (en) Carbon dioxide absorber, methods for its preparation and method for cleaning gas mixtures