JP2000202235A - Sheet-shaped material for removing malodorous gas - Google Patents

Sheet-shaped material for removing malodorous gas

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Publication number
JP2000202235A
JP2000202235A JP11011747A JP1174799A JP2000202235A JP 2000202235 A JP2000202235 A JP 2000202235A JP 11011747 A JP11011747 A JP 11011747A JP 1174799 A JP1174799 A JP 1174799A JP 2000202235 A JP2000202235 A JP 2000202235A
Authority
JP
Japan
Prior art keywords
sheet
activated carbon
filter
phosphoric acid
fiber
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.)
Pending
Application number
JP11011747A
Other languages
Japanese (ja)
Inventor
Takashi Nogi
崇志 野木
Isamu Koyama
勇 小山
Masayoshi Higashihara
優美 東原
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP11011747A priority Critical patent/JP2000202235A/en
Publication of JP2000202235A publication Critical patent/JP2000202235A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a sheet-shaped material for removing malodorous gas capable of easily obtaining the filter having high removing capacity to the malodorous gas and also low in pressure loss when the matter is subjected to fabrication. SOLUTION: This sheet-shaped material is composed of the activated carbon fiber having >=0.7 ml/g fine pore volume and >=2.0 nm average fine pore diameter and a heat fusible fiber, and the constitution ratio is (50:50) to (90:10) by weight. The sheet-shaped matter has <=0.5 mm thickness and keeps >=25 g/m2 phosphoric acid in the sheet.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、フィルター用途、
特にクリーンルーム用フィルター用途に好適な悪臭ガス
除去用シート状物に関するものである。
TECHNICAL FIELD The present invention relates to a filter application,
In particular, the present invention relates to a sheet-like material for removing odorous gas which is suitable for use as a filter for a clean room.

【0002】[0002]

【従来の技術】活性炭繊維を用いたシート状物はよく知
られており、各種有機ガスの除去フィルター用途に利用
されてきた。また、活性炭繊維では物理吸着できないガ
スを除去する目的で、活性炭繊維に薬剤を添着させ、ケ
ミカルフィルター用途にも利用されている。これら、フ
ィルターの形状としては、平板シートと波形状シートを
交互に積み重ね、ハニカム状としたコルゲートフィルタ
ーが低圧力損失であることから多く用いられており、活
性炭繊維からなるシートをこれらの形状に加工して一つ
のフィルターとして作り上げ、半導体工場等のクリーン
ルーム用フィルターとして多く利用され、必要不可欠な
ものとなりつつあるのが現状である。
2. Description of the Related Art Sheets using activated carbon fibers are well known and have been used for filters for removing various organic gases. Further, in order to remove a gas that cannot be physically adsorbed by activated carbon fiber, a chemical is attached to the activated carbon fiber, and it is also used for a chemical filter. As the shape of these filters, a flat corrugated sheet and a corrugated sheet are alternately stacked, and a honeycomb-shaped corrugated filter is often used because of its low pressure loss, and a sheet made of activated carbon fiber is processed into these shapes. At present, it is being used as a filter for clean rooms of semiconductor factories and the like, and is becoming indispensable.

【0003】ケミカルフィルターとしての性能と寿命
は、添着されている薬剤の量に依存することから、高性
能のフィルターを作製するには、より多くの添着剤を保
持したシートが必要となり、添着剤を保持させた活性炭
繊維をより多く持った活性炭繊維シートが必要となる。
しかし、添着剤を保持した活性炭繊維の量を多くする
と、活性炭繊維シートとして保持する添着剤の量は増え
るが、シートの厚みが増大してコルゲートフィルターの
圧力損失が高くなり、フィルターとしての使用に支障を
きたす。特に活性炭繊維シートは、一般的な熱可塑性樹
脂からなる繊維シートと比べると嵩密度が高く、曲げ剛
性も高いため、シート中の繊維が膨らみやすく、シート
の厚みを薄くすることが難しい。そのため厚みを抑える
には、活性炭繊維の量を減らすしかなく、その結果、添
着剤の保持量が少ないシートしか得ることができなかっ
た。
[0003] Since the performance and life as a chemical filter depend on the amount of the adhering chemical, a sheet holding a larger amount of the adhering agent is required to produce a high-performance filter. An activated carbon fiber sheet having more activated carbon fibers holding the carbon fibers is required.
However, when the amount of the activated carbon fiber holding the adsorbent is increased, the amount of the adsorbent held as the activated carbon fiber sheet is increased, but the thickness of the sheet is increased and the pressure loss of the corrugated filter is increased, and the use as a filter is increased. Cause trouble. In particular, the activated carbon fiber sheet has a higher bulk density and a higher flexural rigidity as compared with a fiber sheet made of a general thermoplastic resin, so that the fibers in the sheet easily swell, and it is difficult to reduce the thickness of the sheet. Therefore, the only way to reduce the thickness is to reduce the amount of activated carbon fibers. As a result, only a sheet having a small amount of the adhering agent could be obtained.

【0004】本発明は、このような問題点を解決し、化
学吸着能力が高く、低圧力損失のフィルターを作製する
ことができる悪臭ガス除去用シート状物を提供すること
を技術的な課題とするものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems and to provide a sheet-like material for removing malodorous gas, which is capable of producing a filter having a high chemical adsorption capacity and a low pressure loss. Is what you do.

【0005】[0005]

【課題を解決するための手段】本発明者らは、上記の課
題を解決するために鋭意検討した結果、本発明に到達し
た。すなわち、本発明は、細孔容積が0.7ml/g以
上、平均細孔直径が2.0nm以上の活性炭繊維と熱融
着性繊維とで構成され、その構成比率が重量比で50:
50〜90:10であるシート状物であり、かつ、シー
トの厚みが0.5mm以下で、シート中にリン酸を25
g/m2 以上保持していることを特徴とする悪臭ガス除
去用シート状物を要旨とするものである。
Means for Solving the Problems The present inventors have made intensive studies to solve the above-mentioned problems, and as a result, have reached the present invention. That is, the present invention comprises activated carbon fibers having a pore volume of 0.7 ml / g or more and an average pore diameter of 2.0 nm or more and heat-fusible fibers, and the composition ratio is 50:
It is a sheet-like material having a thickness of 50 to 90:10, and the thickness of the sheet is 0.5 mm or less.
The object of the present invention is to provide a sheet-like material for removing odorous gas, characterized in that it has a g / m 2 or more.

【0006】[0006]

【発明の実施の形態】以下、本発明について詳細に説明
する。まず、熱融着性繊維と共に本発明の悪臭ガス除去
用シート状物を構成する活性炭繊維について説明する。
本発明における活性炭繊維は、ピッチ系、フェノール
系、セルロース系等のものを使用することができるが、
細孔容積が0.7ml/g以上、平均細孔直径が2.0
nm以上であることが必要である。本発明のシート状物
は、後述するようにリン酸を25g/m2 以上保持して
いるものであるが、細孔容積が0.7ml/g未満であ
ったり、平均細孔直径が2.0nm未満になると、活性
炭繊維にリン酸を添着してもその保持量が少なく、圧力
損失を許容できる範囲の厚みのシート状物を作製した
時、シート状物中に存在するリン酸量が少なすぎるの
で、ケミカルフィルターとしての性能と寿命を充分満足
することができず、本発明の目的とするフィルター用の
悪臭ガス除去用シート状物を得ることはできない。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. First, the activated carbon fiber constituting the sheet-like material for removing offensive odor gas of the present invention together with the heat-fusible fiber will be described.
Activated carbon fiber in the present invention, pitch-based, phenol-based, cellulose-based, etc. can be used,
The pore volume is 0.7 ml / g or more and the average pore diameter is 2.0
nm or more. The sheet-like material of the present invention holds phosphoric acid at 25 g / m 2 or more as described later, but has a pore volume of less than 0.7 ml / g or an average pore diameter of 2. When the thickness is less than 0 nm, the amount of phosphoric acid present in the sheet is small when a sheet having a thickness within a range in which pressure loss can be tolerated is small even when phosphoric acid is impregnated into the activated carbon fiber. Since it is too high, the performance and life as a chemical filter cannot be sufficiently satisfied, and the object of the present invention cannot be obtained as a sheet for removing a bad odor gas for a filter.

【0007】次に、活性炭繊維と共に本発明のシート状
物を構成する熱融着性繊維は、シート状の活性炭繊維を
低厚みの状態に形態保持させるため繊維間固定を行うも
のである。活性炭繊維シートは、一般的な熱可塑性樹脂
からなる繊維シートと比べて嵩密度が高く、曲げ剛性も
高いため、シート中の繊維が膨らみやすく、シートの厚
みを薄くすることが難しい。本発明においては、シート
状物の厚みを抑えるため、活性炭繊維と熱融着性繊維を
重量比で50:50〜90:10の割合で用いる必要が
ある。シート状物中に占める熱融着性繊維の重量比率が
50%を超えるとシート状物の厚みを薄くすることはで
きるが、活性炭繊維の比率が少なくなりすぎて、活性炭
繊維の吸着能力と活性炭繊維に保持されるリン酸の量が
減り、ケミカルフィルターとした時に性能と寿命を充分
満足することができないシート状物しか得られない。ま
た、シート状物中に占める熱融着性繊維の重量比率が1
0%を下回ると、活性炭繊維の比率が高くなりすぎてシ
ート状物の厚みが増し、ケミカルフィルターとした時の
圧力損失が高くなる。したがって、活性炭繊維と熱融着
性繊維の重量比率は50:50〜90:10、特に6
5:35〜85:15が好ましい。
[0007] Next, the heat-fusible fibers constituting the sheet-like material of the present invention together with the activated carbon fibers are used to fix the fibers between the activated carbon fibers in order to maintain the shape of the activated carbon fibers in a low thickness state. The activated carbon fiber sheet has a higher bulk density and a higher bending rigidity than a fiber sheet made of a general thermoplastic resin, so that the fibers in the sheet easily swell and it is difficult to reduce the thickness of the sheet. In the present invention, in order to suppress the thickness of the sheet-like material, it is necessary to use the activated carbon fiber and the heat-fusible fiber in a weight ratio of 50:50 to 90:10. If the weight ratio of the heat-fusible fibers in the sheet material exceeds 50%, the thickness of the sheet material can be reduced, but the ratio of the activated carbon fibers becomes too small, and the adsorption capacity of the activated carbon fibers and the activated carbon The amount of phosphoric acid retained in the fiber is reduced, and only a sheet-like material whose performance and life cannot be sufficiently satisfied when a chemical filter is formed can be obtained. Further, the weight ratio of the heat-fusible fibers in the sheet material is 1%.
If it is less than 0%, the ratio of the activated carbon fiber becomes too high, the thickness of the sheet increases, and the pressure loss when a chemical filter is formed increases. Therefore, the weight ratio between the activated carbon fiber and the heat-fusible fiber is 50:50 to 90:10, particularly 6
5:35 to 85:15 is preferred.

【0008】シート状物の形態を保持するためにエマル
ジョンバインダー等の溶液状のバインダー樹脂を用いる
と、活性炭繊維に存在する細孔をバインダーが塞ぐため
好ましくなく、特にリン酸を添着した活性炭繊維の場
合、リン酸とバインダーが反応する可能性もあるので好
ましくない。また、活性炭繊維は、その性状から一般の
合成繊維等と比べ繊維の機械的強力等が低いので、活性
炭繊維を構成繊維とするシート状物も同様に強力が弱い
ものになりがちであり、この欠点を補う点でも、形態保
持と同時に補強繊維としても作用する熱融着性繊維は最
適である。
It is not preferable to use a solution-type binder resin such as an emulsion binder in order to maintain the form of the sheet-like material, since the binder blocks pores existing in the activated carbon fiber. In such a case, phosphoric acid and the binder may react, which is not preferable. Activated carbon fibers also have low mechanical strength and the like as compared with general synthetic fibers and the like due to their properties, so that sheet-like materials having activated carbon fibers as constituent fibers tend to be similarly weak in strength. In terms of compensating for the drawbacks, the heat-fusible fiber which functions as a reinforcing fiber at the same time as retaining the shape is optimal.

【0009】本発明において、熱融着性繊維は、その接
触している活性炭繊維を接触点においてのみ、重合体の
溶融で融着接着させることが好ましい。さらに、鞘成分
に低融点重合体を、芯成分に高融点重合体を配した芯鞘
複合繊維の場合、鞘成分は熱融着による繊維間の接着を
行うが、芯成分は付与された熱に対して劣化や不定型化
することがないので、シート状物を構成する繊維の一つ
となり、シート状物の機械的性能を向上させることから
特に好ましく、その他の二成分系複合繊維も同様な理由
から好適である。
In the present invention, it is preferable that the activated carbon fibers which are in contact with the heat fusible fibers are fused and adhered only at the contact points by melting the polymer. Furthermore, in the case of a core-sheath conjugate fiber in which a low-melting-point polymer is disposed in the sheath component and a high-melting-point polymer is disposed in the core component, the sheath component adheres to each other by heat fusion. Since it does not deteriorate or become irregular, it becomes one of the fibers constituting the sheet-like material, and is particularly preferable because the mechanical performance of the sheet-like material is improved. It is suitable for various reasons.

【0010】また、この熱融着性繊維に用いる重合体
は、繊維形成性、熱融着性、耐薬品性の観点から、ポリ
アミド系、ポリエステル系、ポリオレフィン系重合体が
好ましく、代表的には、ナイロン6、ナイロン46、ナ
イロン66等のポリアミド系重合体、ポリエチレンテレ
フタレ−ト、ポリブチレンテレフタレ−ト、イソフタル
酸共重合ポリエチレンテレフタレ−ト等のポリエステル
系重合体や、ポリエチレン、ポリプロピレン等のポリオ
レフィン系重合体、そして、これら重合体のブレンド物
や、これらの共重合体からなるものも含まれ、本発明の
効果を阻害しない範囲で、艶消し剤、顔料、防炎剤、消
泡剤、帯電防止剤、酸化防止剤、紫外線吸収剤等の任意
の添加剤が添加されたものでもよい。
The polymer used for the heat-fusible fiber is preferably a polyamide-based, polyester-based, or polyolefin-based polymer from the viewpoints of fiber forming properties, heat-fusing properties, and chemical resistance. Polyamide polymers such as nylon 6, nylon 46, nylon 66, etc .; polyester polymers such as polyethylene terephthalate, polybutylene terephthalate, polyethylene terephthalate copolymerized with isophthalic acid; polyethylene, polypropylene, etc. Polyolefin-based polymers, and blends of these polymers, and those composed of these copolymers are also included, as long as the effects of the present invention are not impaired, matting agents, pigments, flame retardants, defoamers Any additive such as an agent, an antistatic agent, an antioxidant, and an ultraviolet absorber may be added.

【0011】本発明のシート状物では、これらの重合体
のうち、一種、もしくは二種から選択された重合体によ
って形成された単一乃至複合形態の熱融着性繊維を使用
するが、熱融着性繊維の繊度は、繊維強力と接着強力の
点から0.5d〜5dが、特に1d〜3dが好ましい。
In the sheet of the present invention, a single or composite heat-fusible fiber formed of one or two of these polymers is used. The fineness of the fusible fiber is preferably from 0.5 d to 5 d, particularly preferably from 1 d to 3 d, from the viewpoint of fiber strength and adhesive strength.

【0012】本発明のシート状物に保持させる薬剤は、
アンモニアガス等の悪臭ガス除去を対象とすることから
リン酸を用いる必要がある。そして、シート状物中にリ
ン酸を25g/m2 以上保持させることがケミカルフィ
ルターとした時の性能の点から重要であり、これを実現
するために、本発明では、前述したように細孔容積が
0.7ml/g以上、平均細孔直径が2.0nm以上の
活性炭繊維を用いるのである。単にシート状物中のリン
酸量を増やすには、リン酸を添着した活性炭繊維の重量
を増やせばよいが、それではシートの厚みが増してしま
い、低圧損のコルゲートフィルターを作製することがで
きない。そこで、本発明では、シート状物中の活性炭繊
維の重量を増やすことなく、添着リン酸量を増やすた
め、リン酸添着に最適な細孔容積が0.7ml/g以
上、平均細孔直径が2.0nm以上の活性炭繊維を使用
することで、従来相反するものであった低厚み、高保持
量の悪臭ガス除去用シート状物とすることができるので
ある。
[0012] The agent held by the sheet of the present invention is
Phosphoric acid must be used because it is intended to remove malodorous gas such as ammonia gas. It is important to keep phosphoric acid in the sheet-like material at 25 g / m 2 or more from the viewpoint of performance when a chemical filter is used, and in order to realize this, in the present invention, as described above, pores are used. Activated carbon fibers having a volume of 0.7 ml / g or more and an average pore diameter of 2.0 nm or more are used. To simply increase the amount of phosphoric acid in the sheet-like material, the weight of the activated carbon fiber impregnated with phosphoric acid may be increased. However, the thickness of the sheet increases, and a corrugated filter with low pressure loss cannot be manufactured. Therefore, in the present invention, since the amount of phosphoric acid to be impregnated is increased without increasing the weight of activated carbon fibers in the sheet-like material, the optimum pore volume for phosphoric acid impregnation is 0.7 ml / g or more, and the average pore diameter is By using activated carbon fibers having a thickness of 2.0 nm or more, it is possible to obtain a sheet having a low thickness and a high retention amount for removing odorous gas, which has been conventionally contradictory.

【0013】図1は、本発明のシート状物をコルゲート
フィルター加工して得られるフィルターの一実施態様を
示す断面図である。図1から明らかなように、本発明の
シート状物を用いたコルゲートフィルターでは、外形が
一定の場合、シート状物の厚みが増すと空気の流路であ
るコルゲートフィルターのセルサイズが小さくなり、圧
力損失が増加する形態になることがわかる。しかし、本
発明では、シート状物の厚みを薄くすることで、空気流
路を大きくした低圧力損失のコルゲートフィルターを提
供することができる。
FIG. 1 is a sectional view showing an embodiment of a filter obtained by corrugating a sheet-like material of the present invention. As is clear from FIG. 1, in the corrugated filter using the sheet-like material of the present invention, when the outer shape is constant, the cell size of the corrugate filter that is the air flow path decreases as the thickness of the sheet-like material increases, It can be seen that the pressure loss increases. However, in the present invention, it is possible to provide a low pressure loss corrugated filter having a large air flow path by reducing the thickness of the sheet.

【0014】次に、本発明の悪臭ガス除去用シート状物
の製造法について説明する。なお、ここで説明する方法
は、本発明のシート状物の製造法の一実施形態にすぎ
ず、何らこれに限定されるものではない。本発明のシー
ト状物を製造するには、まず活性炭繊維と熱融着性繊維
を所定の重量比で混綿した後、ランダムカード、パラレ
ルカード等のカード機を用い、活性炭繊維と熱融着性繊
維からなる不織ウェブを形成する。なおこの際、目付に
応じてクロスラッパー等により不織ウェブをクロスラッ
プさせ、ニードルパンチ装置で機械的に繊維の三次元交
絡を生じさせて一体化させた不織ウェブを形成する方法
も、適宜採用することができる。このようにして得られ
た活性炭繊維と熱融着性繊維とからなる不織ウェブを、
熱融着性繊維の融点以上、(融点+40)℃未満の温度
に設定した乾燥機中を通過させ、熱融着性繊維の熱融着
により不織ウェブ状活性炭繊維の繊維間を固定してシー
ト化を行い、二つのフラットロールからなる一対のロー
ルを備えた熱圧接装置等を用いて厚みを抑えたシート状
物を得る。
Next, a method for producing the sheet material for removing odorous gas of the present invention will be described. Note that the method described here is merely an embodiment of the method for producing a sheet-like material of the present invention, and the present invention is not limited thereto. In order to manufacture the sheet-like material of the present invention, first, activated carbon fibers and heat-fusible fibers are mixed at a predetermined weight ratio, and then, using a card machine such as a random card or a parallel card, the activated carbon fibers and heat-fusible fibers are mixed. Form a nonwoven web of fibers. At this time, the method of cross-lapping the non-woven web with a cross wrapper or the like according to the basis weight and mechanically generating three-dimensional entanglement of the fibers with a needle punch device to form an integrated non-woven web is also appropriate. Can be adopted. A nonwoven web composed of the activated carbon fibers and the heat-fusible fibers thus obtained,
The fiber is passed through a dryer set at a temperature equal to or higher than the melting point of the heat-fusible fiber and lower than (melting point + 40) ° C., and the fibers of the nonwoven web-like activated carbon fiber are fixed by heat-sealing the heat-fusible fiber. The sheet is formed into a sheet, and a sheet-like material having a reduced thickness is obtained by using a thermocompression welding device having a pair of two flat rolls.

【0015】本発明のシート状物にリン酸を保持させる
には、リン酸を添着させた活性炭繊維を用い、上記の製
法でシート状物を得る方法と、上記の製法で製造された
シート状物に後からリン酸を添着させる製法の二通りが
ある。シート状物に後からリン酸を添着させる方法とし
ては、マングル含浸機等を用いてリン酸液中にシート状
物を浸積させる含浸法、コーティングロール等を用いて
リン酸液をシート状物上に塗布するロールコーティング
法、ドクターナイフ等を用いてシート状物上に塗布した
リン酸液を均一にコーティングするナイフコーティング
法、スプレーガン等を用いてリン酸液をシート状物上に
塗布するスプレーコーティング法等が挙げられ、リン酸
液濃度と粘度等により最適な方法を選択し、シート状物
にリン酸を25g/m2 以上保持させることで、目的と
するシート状物を得ることができる。
In order to retain phosphoric acid on the sheet-like material of the present invention, a method of obtaining a sheet-like material by the above-mentioned method using activated carbon fiber impregnated with phosphoric acid, and a method of producing a sheet-like material produced by the above-mentioned method. There are two types of manufacturing methods in which phosphoric acid is later impregnated into the product. Examples of the method of impregnating the sheet material with phosphoric acid later include: an impregnation method in which the sheet material is immersed in a phosphoric acid solution using a mangle impregnating machine or the like; The phosphoric acid solution is applied to the sheet using a roll coating method, a doctor knife or the like, a knife coating method for uniformly coating the phosphoric acid applied on the sheet using a doctor knife, or a spray gun. The most suitable method is selected depending on the concentration of the phosphoric acid solution and the viscosity, etc., and the phosphoric acid is held at 25 g / m 2 or more in the sheet to obtain the desired sheet. it can.

【0016】[0016]

【実施例】次に、本発明を実施例により具体的に説明す
る。なお、実施例において、各特性値の測定は、次によ
うにして行った。 (1) 重合体の融点 パ−キンエルマ−社製DSC−7型の示差走査型熱量計
を用いて、昇温速度20℃/分で測定した融解吸熱ピ−
クの最大値を与える温度を融点とした。 (2) 活性炭繊維の細孔容積と平均細孔直径 日本ベル株式会社製ベルソープ自動ガス吸着装置を用い
て、低温窒素吸着法でBET多点法により、細孔容積は
相対圧1.0で、比表面積(m2/g)は相対圧0.1で
測定し,平均細孔直径は次の式で算出した。 平均細孔直径=細孔容積×4/比表面積 (3) アンモニアガスの濃度 アンモニアガス用の光明理化学工業株式会社製、北川式
ガス検知管を用い測定した値である。 (4) シート状物中のリン酸量 シート状物の1m2 当たり1点が10cm×10cmと
して3点を切り出し、そのシート中のリン酸を400m
lの水で洗い流し、さらにリン酸洗液中に1N−NaO
Hを加え、液のPHを9以上にした後、1N−HClを
用いて逆滴定を行い、求めた値を平均して1m2 当たり
に換算した値である。 (5) シート状物の厚み JIS−L1096に準じて測定した値である。
Next, the present invention will be described in detail with reference to examples. In the examples, the measurement of each characteristic value was performed as follows. (1) Melting point of polymer Melt endothermic peak measured at a heating rate of 20 ° C./min using a DSC-7 type differential scanning calorimeter manufactured by PerkinElmer.
The temperature giving the maximum value of the peak was defined as the melting point. (2) Pore volume and average pore diameter of activated carbon fiber Using a bell soap automatic gas adsorption device manufactured by Japan Bell Co., Ltd., the low pressure nitrogen adsorption method by BET multipoint method, the pore volume is a relative pressure of 1.0, The specific surface area (m 2 / g) was measured at a relative pressure of 0.1, and the average pore diameter was calculated by the following equation. Average pore diameter = pore volume × 4 / specific surface area (3) Concentration of ammonia gas It is a value measured by using a Kitagawa gas detector tube manufactured by Komei Rikagaku Kogyo Co., Ltd. for ammonia gas. (4) 1 point per 1 m 2 of phosphate amount sheet of the sheet-like material is cut out three as 10 cm × 10 cm, 400 meters of phosphoric acid during its seat
1N of NaO in the phosphoric acid washing solution.
After adding H to adjust the pH of the solution to 9 or more, a back titration was performed using 1N-HCl, and the obtained values were averaged and converted per 1 m 2 . (5) Thickness of sheet-like material It is a value measured according to JIS-L1096.

【0017】実施例1 細孔容積が0.8ml/g、平均細孔直径が2.1nm
のピッチ系活性炭繊維と、鞘成分にイソフタル酸を40
モル%共重合した融点110℃の共重合ポリエチレンテ
レフタレート重合体を、芯成分に融点260℃のポリエ
チレンテレフタレート重合体を配した熱融着性繊維(ユ
ニチカ株式会社製 メルティ4080)とを、活性炭繊
維80重量%、熱融着性繊維20重量%の重量比で混綿
した後、パラレルカードで不織ウェブ化し、125℃の
状態に保った乾燥機内を通過させることで鞘成分を溶融
させ、繊維間を固定して目付100g/m2 のシート状
物を得た。次いで、上記のシート状物にスプレーコーテ
ィング法でリン酸を添着し、二つのフラットロールから
なる一対のロールを備えた熱圧接装置にクリアランスを
設け、130℃の温度で熱圧接装置に通して厚さ0.4
5mmのシート状物をとした。
Example 1 The pore volume is 0.8 ml / g and the average pore diameter is 2.1 nm.
Of pitch-based activated carbon fiber and isophthalic acid as a sheath component
Activated carbon fiber 80 was prepared by combining a copolymerized polyethylene terephthalate polymer having a melting point of 110 ° C. obtained by copolymerization with mol% and a heat-fusible fiber (Melty 4080 manufactured by Unitika Ltd.) having a polyethylene terephthalate polymer having a melting point of 260 ° C. as a core component. After blending at a weight ratio of 20% by weight of the heat-fusible fiber to a non-woven web with a parallel card, the sheath component is melted by passing through a dryer kept at 125 ° C. The sheet was fixed to obtain a sheet having a basis weight of 100 g / m 2 . Next, phosphoric acid is applied to the above-mentioned sheet-like material by a spray coating method, a clearance is provided in a thermal pressure welding device having a pair of two flat rolls, and the sheet is passed through the thermal pressure welding device at a temperature of 130 ° C. 0.4
A 5 mm sheet was used.

【0018】得られたシート状物をサイズ15cm×1
5cm×15cmのコルゲートフィルターに作製した
後、風洞試験装置に組み込み、アンモニアガスのフィル
ター入側濃度を1ppm一定に調整し、線速度0.5m
/秒で通気試験を行ってフィルターの出側濃度を測定
し、除去率が90%以上を維持した時間をガス除去能力
として評価した。
The obtained sheet is sized 15 cm × 1
After producing a 5 cm x 15 cm corrugated filter, it was incorporated into a wind tunnel tester, the concentration of ammonia gas on the filter inlet side was adjusted to a constant 1 ppm, and the linear velocity was 0.5 m
The air outlet test was carried out at a rate of 1 hour / second to measure the outlet concentration of the filter.

【0019】実施例2 活性炭繊維を、細孔容積が1.0ml/g、平均細孔直
径が3.0nmのものに変更した以外は実施例1と同様
に行って、目付80g/m2 、厚さ0.3mmのシート
状物とした後、フィルターを作製し、実施例1と同じ試
験を行って、フィルターのガス除去能力を評価した。
Example 2 The same procedure as in Example 1 was carried out except that the activated carbon fibers were changed to those having a pore volume of 1.0 ml / g and an average pore diameter of 3.0 nm, and a basis weight of 80 g / m 2 , After forming a sheet having a thickness of 0.3 mm, a filter was prepared, and the same test as in Example 1 was performed to evaluate the gas removing ability of the filter.

【0020】比較例1 活性炭繊維を、細孔容積が0.5ml/g、平均細孔直
径が1.9nmのものに変更した以外は実施例1と同様
に行って、目付80g/m2 、厚さ0.55mmのシー
ト状物とした後、フィルターを作製し、実施例1と同じ
試験を行って、フィルターのガス除去能力を評価した。
Comparative Example 1 The same procedure as in Example 1 was repeated except that the activated carbon fiber was changed to one having a pore volume of 0.5 ml / g and an average pore diameter of 1.9 nm, and the basis weight was 80 g / m 2 , After forming a sheet having a thickness of 0.55 mm, a filter was prepared, and the same test as in Example 1 was performed to evaluate the gas removing ability of the filter.

【0021】比較例2 活性炭繊維を、細孔容積が0.3ml/g、平均細孔直
径が1.7nmのものに変更した以外は実施例1と同様
に行って、目付100g/m2 、厚さ0.7mmのシー
ト状物とした後、フィルターを作製し、実施例1と同じ
試験を行って、フィルターのガス除去能力を評価した。
実施例1〜2と比較例1〜2で得られたシート状物の性
状と、フィルターのガス除去能力の評価結果を併せて表
1に示す。
Comparative Example 2 The same procedure as in Example 1 was carried out except that the activated carbon fiber was changed to one having a pore volume of 0.3 ml / g and an average pore diameter of 1.7 nm, and the basis weight was 100 g / m 2 , After forming a sheet having a thickness of 0.7 mm, a filter was prepared, and the same test as in Example 1 was performed to evaluate the gas removing ability of the filter.
Table 1 also shows the properties of the sheet-like materials obtained in Examples 1 and 2 and Comparative Examples 1 and 2, and the evaluation results of the gas removal ability of the filter.

【0022】[0022]

【表1】 [Table 1]

【0023】表1から明らかなように、実施例1〜2で
得られたシート状物は、比較例1〜2のものより薄く
て,かつ、リン酸の保持量が多いので、比較例1〜2の
フィルターよりアンモニアガスの90%除去時間が長
く、悪臭ガスに対して高い除去能力を示すフィルターで
あった。
As is clear from Table 1, the sheet-like materials obtained in Examples 1 and 2 are thinner than those of Comparative Examples 1 and 2 and have a larger amount of retained phosphoric acid. The filter has a longer removal time of 90% of the ammonia gas than the filters of Nos. 2 and 3, and has a high ability to remove odorous gas.

【0024】[0024]

【発明の効果】本発明の悪臭ガス除去用シート状物を成
形加工すれば、悪臭ガスに対して高い除去能力を有し、
かつ低圧力損失のフィルターを容易に得ることが可能と
なる。
According to the present invention, if the sheet-like material for removing odorous gas of the present invention is formed and processed, it has a high ability to remove odorous gas,
In addition, a filter having a low pressure loss can be easily obtained.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の悪臭ガス除去用シート状物によって形
成されたコルゲートフィルターの一実施態様を示す断面
図である。
FIG. 1 is a cross-sectional view showing one embodiment of a corrugated filter formed by the sheet-like material for removing malodorous gas of the present invention.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D002 AA13 AB02 AC10 BA03 BA04 CA07 DA26 DA44 EA06 GA01 GA02 GB01 GB02 GB03 GB04 GB08 GB09 GB12 HA03 4D012 BA03 CA09 CA10 CB02 CB03 CE02 CE03 CF02 CF03 CF04 CF05 CG04 CG05 CK05  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4D002 AA13 AB02 AC10 BA03 BA04 CA07 DA26 DA44 EA06 GA01 GA02 GB01 GB02 GB03 GB04 GB08 GB09 GB12 HA03 4D012 BA03 CA09 CA10 CB02 CB03 CE02 CE03 CF02 CF03 CF04 CF05 CG04 CG05 CK05

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 細孔容積が0.7ml/g以上、平均細
孔直径が2.0nm以上の活性炭繊維と熱融着性繊維と
で構成され、その構成比率が重量比で50:50〜9
0:10であるシート状物であり、かつ、シートの厚み
が0.5mm以下で、シート中にリン酸を25g/m2
以上保持していることを特徴とする悪臭ガス除去用シー
ト状物。
1. An activated carbon fiber having a pore volume of 0.7 ml / g or more and an average pore diameter of 2.0 nm or more and a heat-fusible fiber, and the composition ratio is 50:50 by weight. 9
0:10, the sheet thickness is 0.5 mm or less, and phosphoric acid in the sheet is 25 g / m 2.
A sheet-like material for removing odorous gas, which is held as described above.
JP11011747A 1999-01-20 1999-01-20 Sheet-shaped material for removing malodorous gas Pending JP2000202235A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11011747A JP2000202235A (en) 1999-01-20 1999-01-20 Sheet-shaped material for removing malodorous gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11011747A JP2000202235A (en) 1999-01-20 1999-01-20 Sheet-shaped material for removing malodorous gas

Publications (1)

Publication Number Publication Date
JP2000202235A true JP2000202235A (en) 2000-07-25

Family

ID=11786621

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11011747A Pending JP2000202235A (en) 1999-01-20 1999-01-20 Sheet-shaped material for removing malodorous gas

Country Status (1)

Country Link
JP (1) JP2000202235A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017047420A (en) * 2004-11-05 2017-03-09 ドナルドソン カンパニー,インコーポレイティド Filter medium
US10610813B2 (en) 2004-11-05 2020-04-07 Donaldson Company, Inc. Filter medium and breather filter structure

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017047420A (en) * 2004-11-05 2017-03-09 ドナルドソン カンパニー,インコーポレイティド Filter medium
US10610813B2 (en) 2004-11-05 2020-04-07 Donaldson Company, Inc. Filter medium and breather filter structure
USRE49097E1 (en) 2004-11-05 2022-06-07 Donaldson Company, Inc. Filter medium and structure
US11504663B2 (en) 2004-11-05 2022-11-22 Donaldson Company, Inc. Filter medium and breather filter structure

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