JPH0317952B2 - - Google Patents

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Publication number
JPH0317952B2
JPH0317952B2 JP62071140A JP7114087A JPH0317952B2 JP H0317952 B2 JPH0317952 B2 JP H0317952B2 JP 62071140 A JP62071140 A JP 62071140A JP 7114087 A JP7114087 A JP 7114087A JP H0317952 B2 JPH0317952 B2 JP H0317952B2
Authority
JP
Japan
Prior art keywords
cellulose fibers
copper
hydroxide
cellulose
sodium hydroxide
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.)
Expired - Lifetime
Application number
JP62071140A
Other languages
Japanese (ja)
Other versions
JPS63235571A (en
Inventor
Yosuke Takai
Makoto Ootaguro
Yoshito Komatsu
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.)
Daiwa Boseki KK
Original Assignee
Daiwa Boseki KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daiwa Boseki KK filed Critical Daiwa Boseki KK
Priority to JP62071140A priority Critical patent/JPS63235571A/en
Publication of JPS63235571A publication Critical patent/JPS63235571A/en
Publication of JPH0317952B2 publication Critical patent/JPH0317952B2/ja
Granted legal-status Critical Current

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  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は消臭機能を有するセルロース繊維の製
造方法、詳しくは化学的活性に富んだ水酸化銅を
セルロース繊維に担持せしめた消臭性繊維の製法
に関する。 (従来の技術) 従来、硫化水素、アンモニア、ホルマリン等に
よる悪臭、有毒ガスの除去方法として高温(650
〜800℃)で燃焼し、水蒸気、炭酸ガスなどの無
臭、無害な物質に分解する方法、触媒を使用し、
250〜300℃で酸化処理する触媒燃焼法があるが、
これら燃焼法は大規模な設備を要し、大量のガス
処理を行う産業用施設以外ではコストが高くつく
欠点があつた。 その他コストが比較的安い簡単な方法として活
性炭、ゼオライト等の吸着剤で悪臭物質を吸着す
る方法や、悪臭より強い芳香により悪臭を感じさ
せなくするマスキング法があるが、これらは強い
臭気には効果がなく、広域の消臭にも不適であ
る。またこれらの消臭剤は粉状或いは液状であ
り、使用にあたり適当な容器に納めるか、不織
布、紙、布等に含浸させている。しかし容器に納
めることにより悪臭気体との接触面積の減少によ
る効果の減少、或いは不織布等への付着力の弱さ
による効果の持続性の減少といつた欠点があつた
のである。 本発明は消臭効果の高い水酸化銅を繊維に強固
に担持させ、上述の欠点を解消した消臭性繊維の
製法に関する。 従来、水酸化銅の持つ殺菌力に着目し、これを
セルロース繊維に担持させた例が特開昭54−
160900号公報が知られているが、目的が殺菌性繊
維の製造であるため、銅の担持量は微量(実施例
ではセルロース繊維1g当り9〜31mg)でも効果
があるが、本発明の目的とする消臭性繊維は長時
間にわたり効果を持続させるために、銅をもつと
多量に担持させる必要がある。さらに銅を担持し
たあとのセルロース繊維の強力が低下していては
せつかく消臭性能を付与しても実用面で制約をう
けることになる。 (発明が解決しようとする問題点) 本発明は水酸化銅をセルロース繊維に多量に担
持せしめ、しかもセルロース繊維の強度低下は極
力小さくすることを目的とする消臭性セルロース
繊維の製造方法である。 前述の特開昭54−160900公報にも記されている
ように、水酸化銅は極めて水溶性が悪く、水酸化
ナトリウムのような強アルカリにわずかに溶ける
が、その溶解量は4規定水酸化ナトリウム水溶液
で850ppmである。そしてセルロースの強度低下
を防ぐため4規定以上の水酸化ナトリウム水溶液
は好ましくないとしている。 しかし本発明においては、セルロース繊維の強
力低下を強力防ぎたいこと、及び使用するセルロ
ース繊維は繊維長、デニール等の繊維形態が自由
に変えられ、所望する製品に応じて適切な加工が
し易いことから、再生セルロースが好ましい素材
であるという事情がある。このため再生セルロー
ス繊維の強力低下が比較的少ない範囲にアルカリ
濃度を設定しなければならなかつた。 このような条件下で、本発明者等は多量の水酸
化銅をセルロース繊維に担持させることに成功し
たのである。 (問題点を解決するための手段) 本発明者等は先に本発明と同様の目的で水酸化
銅又は酸化銅を使用し、セルロース繊維に水酸化
銅を多量に担持させる方法について出願した(特
願昭61−78830)が引続き研究の結果塩基性炭酸
銅を用いてもセルロース繊維に水酸化銅を担持し
得ることを知つた。 塩基性炭酸銅は水酸化銅と炭酸銅の混合物であ
り、天然にはクジヤク石として知られているが、
その組成は一定ではなく、文献により数種
CuCO3・Cu(OH)2,CuCO3・3Cu(OH2)等と記
されている。本明細書ではCuCO3・nCu(OH)2
表示する。塩基性炭酸銅が水酸化ナトリウム水溶
液に溶解する反応式は水酸化ナトリウムが大過剰
とすると CuCO3・nC(OH)2+2(n+2)NaOH →(n+1)[Cu(OH)2- 4・2Na+]+Na2+ 2
・CO2- 3 と考えられ、セルロースとの反応は水酸化銅を用
いたセルロース・銅配位反応と同一の反応である
と思われる。 本発明は0.5〜2.5規定の水酸化ナトリウム水溶
液又は水酸化カリウム水溶液に塩基性炭酸銅の粉
状物を0.5〜50g/の割合で混合分散させ、こ
の混合分散液にセルロース繊維を浸漬して塩基性
炭酸銅の粉状物をセルロース繊維に吸着させるこ
とにより、水酸化銅イオン錯体をセルロース分子
に化学結合させることを特徴とする消臭性セルロ
ース繊維の製造方法である。 使用するセルロース繊維はあらかじめアルカリ
水溶液で前処理し、繊維中に充分アルカリ水溶液
を浸透させることが望ましい。例えば天然セルロ
ース繊維を60℃の0.5規定水酸化ナトリウム水溶
液に0.5〜1.0時間浸漬すればセルロース繊維は充
分に膨潤して付着している油脂分が除去され、セ
ルロース分子に水酸化銅が反応し易くなる。 また再生セルロース繊維を使用する場合は、再
生セルロース繊維は紡糸工程上硫化物が付着しや
すいので、アルカリ前処理液中に少量の水酸化第
二銅を添加しておくと、硫化物は硫化銅として沈
殿し除去することができる。 塩基性炭酸銅を分散させるアルカリ水溶液は水
酸化ナトリウム又は水酸化カリウムの水溶液を用
いるが、その濃度はセルロース繊維を過度に分解
しない程度に2.5規程以下でなければならない。
また低すぎると、塩基性炭酸銅の分解が進まず、
水酸化銅イオン錯体を充分に供給することができ
ないので少なくとも0.5規定以上が必要である。 塩基性炭酸銅の量は50g/より多いとアルカ
リ水溶液中で均一で分散せず、セルロース繊維へ
付着しない量が多くなつて無駄である。また0.5
g/より少ない量ではセルロース繊維へ付着す
る粉状物の量が充分でなく、水酸化銅イオン錯体
を大量にセルロース繊維に結合させるためには、
長時間の反応時間が必要になり好ましくない。 このようなアルカリ性水溶液中に塩基性炭酸銅
は粘着性粒子となつて懸濁液を作り、そこにセル
ロース繊維を投入すると粘着性粒子はセルロース
繊維の周囲に凝集付着する。この付着した塩基性
炭酸銅からセルロース繊維の表面に銅イオン錯体
Cu(OH)4が供給され、これがセルロース繊維と
次のように化学結合しているものと思われる。 セルロース繊維に銅イオン錯体が充分に結合し
た後、余分の塩基性炭酸銅の粒子を取除くため、
全体を搾水し、水中に放置する。このとき水温が
高いほど粒子の粘着性は低下し、水温50℃以上で
は約10分でほぼ完全に脱落する。搾水は遠心脱水
機を使い、充分にアルカリ水溶液を除去する。搾
水後もセルロース繊維はアルカリ水溶液を吸収し
ており、これを水中に放置しても繊維周辺のPH値
はアルカリ性を示すが、浴比を1:50以上にし、
水中をゆるく撹拌してやれば塩基性炭酸銅の粒子
は容易に脱落する。 (発明の作用) 本発明方法による銅イオン錯体のセルロース繊
維への担持は先に出願した水酸化銅又は酸化銅を
使う方法(特願昭61−78830)よりも担持反応が
早く、かつ銅担持も高い。 セルロース繊維に結合した銅イオン錯体は悪臭
物質の元になるアンモニア分子、硫黄イオン、酸
性基と化学反応を起こし、これらを含む悪臭物質
を分解するので、アンモニア、硫化水素、硫黄酸
化物、ホルマリン等の消臭効果をもつている。 (実施例) (1) 5デニールのビスコースレーヨン綿250gを
前処理として、水酸化第二銅1gを添加した60
℃の0.5規定水酸化ナトリウム水溶液5中に
浸漬した。1時間後このレーヨン綿を手絞り
し、もう一度同一の処理を繰り返した後遠心脱
水して水酸化ナトリウム水溶液を含んだ精練綿
を得た。 次にこの精練したレーヨン綿250gを塩基性
炭酸銅75gと共に1.5規定の水酸化ナトリウム
水溶液5中に少量づつ分散させながら投入
し、室温で放置した。レーヨン綿は徐々に青色
に染まり、24時間後脱水、水洗いして80℃で3
時間乾燥した、得られた青色レーヨン綿の銅含
有率は12.4%であつた。 (2) 実施例1と同様にして得られた精練綿250g
を塩基性炭酸銅75gと共に1.0規定の水酸化ナ
トリウム水溶液5中に少量づつ分散させなが
ら投入し、室温で放置した。レーヨン綿は徐々
に青色に染まり、24時間後脱水、水洗いして80
℃で3時間乾燥した。得られた青色レーヨン綿
の銅含有率は5.8%であつた。 (3) 実施例1と同様にして得られた精練綿250g
を塩基性炭酸銅75gと共に0.5規定の水酸化ナ
トリウム水溶液5中に少量づつ分散させ室温
で24時間放置した後、脱水、水洗いし80℃で3
時間乾燥した。得られた青色レーヨン綿の銅含
有率は3.7%であつた。 (4) 実施例1と同様にして得られた精練綿250g
を塩基性、炭酸銅75gと共に2.5規定の水酸化
ナトリウム水溶液5中に少量づつ分散させ室
温で10時間放置した後、脱水、水洗いし80℃で
3時間乾燥した。得られた青色レーヨン綿の銅
含有率は17.0%であつた。 (5) 実施例1において青色に染まつたレーヨンの
脱水前に、その一部を取り、手絞りした後1.5
規定の水酸化ナトリウム水溶液に浸漬し、60℃
で6時間加熱した。水洗い、乾燥後の青色レー
ヨン綿の銅含有率は12.8%であつた。 (6) 実施例1において水酸化ナトリウム水溶液を
水酸化カリウム水溶液に替えた他に全く同一の
方法で青色レーヨン綿を得た。 銅の含有率は、11.9%であつた。 (発明の効果) 実施例1で得られた水酸化銅担持レーヨン綿
0.3gを第1図に示すように内径100mmのガラス管
1内にゆるく詰め、これをゴム栓2を通して100
ml中のフラスコ3の口に固定した。フラスコ3内
にはあらかじめ悪臭ガス発生源物質4を少量入れ
ておき、フラスコ3の底を加熱するか、あるいは
化学反応によつてガスを発生させガラス管1内に
導きガスを水酸化銅担持レーヨン綿5に接触させ
た。数種類の悪臭ガス発生物質(表−1に示す)
につき、各々ガス発生後ガラス管の出口で臭気を
嗅いだが悪臭物質特有の臭気は感じられなかつ
た。このうちアルデヒド類についてはレーヨン綿
5をあらかじめ0.2規定の水酸化ナトリウム水溶
液で湿潤させて使用した。 【表】
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a method for producing cellulose fibers having a deodorizing function, and more specifically to a method for producing deodorizing fibers in which cellulose fibers are made to support chemically active copper hydroxide. Concerning the manufacturing method. (Conventional technology) Conventionally, high temperature (650° C.
Using a catalyst, a method that burns at a temperature of ~800℃) and decomposes it into odorless and harmless substances such as water vapor and carbon dioxide,
There is a catalytic combustion method that performs oxidation treatment at 250-300℃.
These combustion methods require large-scale equipment and have the disadvantage of being expensive for use in facilities other than industrial facilities that process large amounts of gas. Other relatively cheap and simple methods include adsorbing malodorous substances with adsorbents such as activated carbon and zeolite, and masking methods that eliminate the perception of malodors using aromas that are stronger than the malodor, but these methods are effective against strong odors. Therefore, it is not suitable for deodorizing a wide area. These deodorants are in powder or liquid form, and are stored in a suitable container or impregnated into nonwoven fabric, paper, cloth, etc. before use. However, when placed in a container, there were drawbacks such as a decrease in effectiveness due to a decrease in the contact area with foul-smelling gases, and a decrease in the sustainability of the effect due to weak adhesion to nonwoven fabrics, etc. The present invention relates to a method for producing deodorizing fibers that eliminate the above-mentioned drawbacks by firmly supporting copper hydroxide, which has a high deodorizing effect, on fibers. In the past, an example of focusing on the bactericidal power of copper hydroxide and supporting it on cellulose fibers was published in Japanese Patent Application Laid-Open No. 1973-
No. 160900 is known, but since the purpose is to produce bactericidal fibers, even a small amount of supported copper (9 to 31 mg per 1 g of cellulose fiber in the examples) is effective, but this does not meet the purpose of the present invention. In order for the deodorizing fiber to maintain its effect over a long period of time, it is necessary to carry a large amount of copper. Furthermore, if the strength of the cellulose fibers after carrying copper is reduced, even if deodorizing performance is imparted, practicality will be limited. (Problems to be Solved by the Invention) The present invention is a method for producing deodorizing cellulose fibers, the purpose of which is to carry a large amount of copper hydroxide on cellulose fibers, and to minimize the decrease in strength of the cellulose fibers. . As stated in the above-mentioned Japanese Patent Application Laid-Open No. 160900/1983, copper hydroxide has extremely poor water solubility and is slightly soluble in strong alkalis such as sodium hydroxide, but the amount dissolved in 4N hydroxide is It is 850ppm in sodium aqueous solution. In order to prevent a decrease in the strength of cellulose, it is said that an aqueous solution of sodium hydroxide with a concentration of 4N or higher is not preferable. However, in the present invention, it is desired to strongly prevent a decrease in the strength of cellulose fibers, and the cellulose fibers used can be freely changed in fiber form such as fiber length and denier, and can be easily processed appropriately according to the desired product. Therefore, regenerated cellulose is a preferred material. For this reason, it was necessary to set the alkali concentration within a range in which the strength of the regenerated cellulose fibers is relatively small. Under such conditions, the present inventors succeeded in supporting a large amount of copper hydroxide on cellulose fibers. (Means for Solving the Problems) The present inventors previously filed an application for a method for using copper hydroxide or copper oxide to support a large amount of copper hydroxide on cellulose fibers for the same purpose as the present invention ( As a result of continued research in Japanese Patent Application No. 61-78830, it was discovered that copper hydroxide could be supported on cellulose fibers even when basic copper carbonate was used. Basic copper carbonate is a mixture of copper hydroxide and copper carbonate, and is known in nature as pythonite.
Its composition is not constant, and there are several types according to the literature.
It is written as CuCO 3・Cu (OH) 2 , CuCO 3・3Cu (OH 2 ), etc. In this specification, it is expressed as CuCO3.nCu (OH) 2 . The reaction formula for basic copper carbonate to dissolve in an aqueous sodium hydroxide solution is CuCO 3・nC(OH) 2 +2(n+2)NaOH → (n+1)[Cu(OH) 2- 4・2Na, assuming that sodium hydroxide is in large excess. + ]+Na 2+ 2
・It is thought to be CO 2- 3 , and its reaction with cellulose is thought to be the same as the cellulose-copper coordination reaction using copper hydroxide. The present invention involves mixing and dispersing basic copper carbonate powder in a 0.5 to 2.5 N aqueous sodium hydroxide solution or potassium hydroxide aqueous solution at a ratio of 0.5 to 50 g/distance, and immersing cellulose fibers in this mixed dispersion to form a base. This method for producing deodorizing cellulose fibers is characterized in that a copper hydroxide ion complex is chemically bonded to cellulose molecules by adsorbing powdered copper carbonate onto cellulose fibers. It is desirable that the cellulose fibers used be pretreated with an aqueous alkaline solution to allow the aqueous alkaline solution to sufficiently penetrate into the fibers. For example, if natural cellulose fibers are immersed in a 0.5N sodium hydroxide aqueous solution at 60°C for 0.5 to 1.0 hours, the cellulose fibers will swell sufficiently, the fats and oils attached will be removed, and copper hydroxide will easily react with the cellulose molecules. Become. In addition, when using regenerated cellulose fibers, since sulfides tend to adhere to regenerated cellulose fibers during the spinning process, adding a small amount of cupric hydroxide to the alkaline pretreatment solution will remove sulfides from copper sulfide. It can be precipitated and removed as As the aqueous alkaline solution for dispersing basic copper carbonate, an aqueous solution of sodium hydroxide or potassium hydroxide is used, and its concentration must be 2.5 or less so as not to excessively decompose cellulose fibers.
Also, if the temperature is too low, the decomposition of basic copper carbonate will not proceed,
Since a sufficient amount of copper hydroxide ion complex cannot be supplied, at least 0.5 normality is required. If the amount of basic copper carbonate is more than 50 g, it will not be uniformly dispersed in the alkaline aqueous solution and will not adhere to the cellulose fibers, resulting in a wasteful amount. Also 0.5
If the amount is less than 1 g/g, the amount of powdery substances adhering to the cellulose fibers will not be sufficient, and in order to bond a large amount of copper hydroxide ion complex to the cellulose fibers,
This is not preferable because it requires a long reaction time. Basic copper carbonate becomes sticky particles in such an alkaline aqueous solution to form a suspension, and when cellulose fibers are introduced into the suspension, the sticky particles coagulate and adhere around the cellulose fibers. Copper ion complexes are formed on the surface of cellulose fibers from this attached basic copper carbonate.
Cu(OH) 4 is supplied and seems to be chemically bonded to the cellulose fibers as follows. After the copper ion complex has fully bonded to the cellulose fibers, in order to remove excess basic copper carbonate particles,
Squeeze out the whole thing and leave it in the water. At this time, the higher the water temperature, the lower the adhesion of the particles, and if the water temperature is 50°C or higher, they will fall off almost completely in about 10 minutes. For water extraction, use a centrifugal dehydrator to thoroughly remove the alkaline aqueous solution. Cellulose fibers still absorb alkaline aqueous solutions even after watering, and even if they are left in water, the PH value around the fibers remains alkaline, but if the bath ratio is set to 1:50 or higher,
If the water is gently stirred, the basic copper carbonate particles will easily fall off. (Action of the invention) The method of the present invention supports the copper ion complex on the cellulose fibers, and the supporting reaction is faster than the previously applied method using copper hydroxide or copper oxide (Japanese patent application No. 61-78830). It's also expensive. Copper ion complexes bonded to cellulose fibers cause chemical reactions with ammonia molecules, sulfur ions, and acidic groups, which are the sources of malodorous substances, and decompose malodorous substances that contain these substances, such as ammonia, hydrogen sulfide, sulfur oxides, formalin, etc. It has a deodorizing effect. (Example) (1) 250g of 5 denier viscose rayon cotton was pretreated and 1g of cupric hydroxide was added.
It was immersed in a 0.5N aqueous sodium hydroxide solution at 5°C. One hour later, this rayon cotton was hand-wrung, and the same treatment was repeated once more, followed by centrifugal dehydration to obtain scouring cotton containing an aqueous sodium hydroxide solution. Next, 250 g of this scoured rayon cotton was dispersed little by little into a 1.5N aqueous sodium hydroxide solution 5 along with 75 g of basic copper carbonate, and the mixture was allowed to stand at room temperature. The rayon cotton gradually turns blue, and after 24 hours, it is dehydrated, washed with water, and heated at 80℃ for 3 days.
The copper content of the obtained blue rayon cotton, which was dried for an hour, was 12.4%. (2) 250g of scouring cotton obtained in the same manner as in Example 1
and 75 g of basic copper carbonate were added to a 1.0N aqueous sodium hydroxide solution 5 while being dispersed little by little, and the mixture was allowed to stand at room temperature. The rayon cotton gradually turns blue, and after 24 hours, it is dehydrated and washed with water.
It was dried at ℃ for 3 hours. The copper content of the obtained blue rayon cotton was 5.8%. (3) 250g of scouring cotton obtained in the same manner as in Example 1
was dispersed little by little in a 0.5 N aqueous sodium hydroxide solution 5 with 75 g of basic copper carbonate, left at room temperature for 24 hours, dehydrated, washed with water, and heated to 80°C for 3 hours.
Dry for an hour. The copper content of the obtained blue rayon cotton was 3.7%. (4) 250g of scouring cotton obtained in the same manner as in Example 1
was dispersed little by little in a 2.5 N aqueous sodium hydroxide solution 5 together with 75 g of basic copper carbonate, left to stand at room temperature for 10 hours, dehydrated, washed with water, and dried at 80° C. for 3 hours. The copper content of the obtained blue rayon cotton was 17.0%. (5) In Example 1, before dehydrating the blue-dyed rayon, take a part of it and squeeze it by hand.
Immerse in specified sodium hydroxide aqueous solution at 60℃
It was heated for 6 hours. The copper content of the blue rayon cotton after washing and drying was 12.8%. (6) Blue rayon cotton was obtained in exactly the same manner as in Example 1 except that the sodium hydroxide aqueous solution was replaced with a potassium hydroxide aqueous solution. The copper content was 11.9%. (Effect of the invention) Copper hydroxide-supported rayon cotton obtained in Example 1
As shown in Figure 1, loosely pack 0.3 g into a glass tube 1 with an inner diameter of 100 mm, and insert it through a rubber stopper 2.
ml was fixed at the mouth of flask 3. A small amount of a foul-smelling gas generating substance 4 is placed in the flask 3 in advance, and the bottom of the flask 3 is heated or a gas is generated through a chemical reaction and the gas is introduced into the glass tube 1 using copper hydroxide-supported rayon. It was brought into contact with cotton 5. Several types of foul-smelling gas generating substances (shown in Table 1)
After each gas was generated, the odor was smelled at the outlet of the glass tube, but no odor peculiar to malodorous substances was detected. For aldehydes, rayon cotton 5 was pre-wetted with a 0.2N aqueous sodium hydroxide solution. 【table】

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明の効果を確認するための器具の正
面図である。 図において、1……ガラス管、2……ゴム栓、
3……フラスコ、4……悪臭ガス発生源物質、5
……水酸化銅担持レーヨン綿。
The drawing is a front view of an instrument for confirming the effects of the present invention. In the figure, 1...Glass tube, 2...Rubber stopper,
3...Flask, 4...Offensive gas generating substance, 5
... Rayon cotton carrying copper hydroxide.

Claims (1)

【特許請求の範囲】[Claims] 1 0.5〜2.5規定の水酸化ナトリウム水溶液又は
水酸化カリウム水溶液に塩基性炭酸銅の粉状物を
0.5〜50g/の割合で混合分散させ、この混合
分散液にセルロース繊維を浸漬して塩基性炭酸銅
の粉状物をセルロース繊維に吸着させることによ
り、水酸化銅イオン錯体をセルロース分子に化学
結合させることを特徴とする消臭性セルロース繊
維の製造方法。
1 Add basic copper carbonate powder to a 0.5-2.5N aqueous sodium hydroxide solution or aqueous potassium hydroxide solution.
The copper hydroxide ion complex is chemically bonded to the cellulose molecules by mixing and dispersing it at a ratio of 0.5 to 50 g/distance and immersing the cellulose fibers in this mixed dispersion to adsorb the basic copper carbonate powder onto the cellulose fibers. A method for producing deodorizing cellulose fiber, characterized by:
JP62071140A 1987-03-24 1987-03-24 Production of deodorizing cellulose fiber Granted JPS63235571A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62071140A JPS63235571A (en) 1987-03-24 1987-03-24 Production of deodorizing cellulose fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62071140A JPS63235571A (en) 1987-03-24 1987-03-24 Production of deodorizing cellulose fiber

Publications (2)

Publication Number Publication Date
JPS63235571A JPS63235571A (en) 1988-09-30
JPH0317952B2 true JPH0317952B2 (en) 1991-03-11

Family

ID=13451984

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62071140A Granted JPS63235571A (en) 1987-03-24 1987-03-24 Production of deodorizing cellulose fiber

Country Status (1)

Country Link
JP (1) JPS63235571A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2525643B2 (en) * 1988-06-23 1996-08-21 株式会社興人 Method for producing deodorant fiber
JP2007069018A (en) * 2006-11-27 2007-03-22 Kohjin Co Ltd Material having deodorizing function and method for producing the same
JP2013099483A (en) * 2011-11-09 2013-05-23 Suminoe Textile Co Ltd Organic acid smell removing filter
JP7209406B1 (en) * 2022-07-29 2023-01-20 昭人 ▲高▼宮 Portable simple smell comparison box
JP7278014B1 (en) * 2022-07-29 2023-05-19 昭人 ▲高▼宮 Portable simple smell comparison box

Also Published As

Publication number Publication date
JPS63235571A (en) 1988-09-30

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