JPS6211582B2 - - Google Patents

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Publication number
JPS6211582B2
JPS6211582B2 JP8020084A JP8020084A JPS6211582B2 JP S6211582 B2 JPS6211582 B2 JP S6211582B2 JP 8020084 A JP8020084 A JP 8020084A JP 8020084 A JP8020084 A JP 8020084A JP S6211582 B2 JPS6211582 B2 JP S6211582B2
Authority
JP
Japan
Prior art keywords
carrier
catalyst
activated carbon
supported
bentonite
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
Application number
JP8020084A
Other languages
Japanese (ja)
Other versions
JPS60224483A (en
Inventor
Shigeo Ichise
Kenichiro Sugimori
Hajime Matsushita
Hiroshi Ichise
Akira Izumi
Shigeo Ishiguro
Ayumi Nakanishi
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.)
Japan Tobacco Inc
Original Assignee
Japan Tobacco Inc
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 Japan Tobacco Inc filed Critical Japan Tobacco Inc
Priority to JP8020084A priority Critical patent/JPS60224483A/en
Publication of JPS60224483A publication Critical patent/JPS60224483A/en
Publication of JPS6211582B2 publication Critical patent/JPS6211582B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、たばこの香喫味に悪影響を及ぼすこ
となく喫煙時に発生するたばこ煙から一酸化炭素
を選択的に除去する除去剤に関する。 一般に、炭素や含炭素化合物の不完全燃焼によ
つて発生する一酸化炭素(以下単にCOともい
う)は、血液中のヘモグロビンと強固に結合し、
血液の酸素吸収及び運搬の役割を著しく阻害する
ため、頭痛、めまいなどの急性中毒症状をひき起
し、甚だしい場合には死に至らしめる。又、CO
に長期的に暴露された場合には慢性心臓疾患を喚
起するといわれている。 このCOは喫煙者がたばこを喫煙した際に直接
吸入する煙いわゆる主流煙中にも数パーセント含
有されており、これは人体の肺に達するまでに同
時に吸入される空気により大幅に希釈されるもの
の、喫煙者の血中CO結合ヘモグロビンの慢性的
な濃度上昇に寄与しているとされ、たばこ煙中か
らのCOの低減は喫煙者の健康上の観点から早急
に解決をはかるべき重要な課題とされている。 〔従来の技術〕 従来、かかる観点からたばこ主流煙中のCO濃
度を低減させようとする試みが盛んに行なわれ、
特許明細書等において多くの提案がなされてい
る。 これらの提案は大別すると以下のように分類す
ることができる。 (1) COの生成の少ない原料を選択して使用する
方法。 (2) フイルター部分に開孔を設け、あるいは巻紙
に高気孔度のものを使用してCOの生成を抑制
したり、生成したCOを巻紙からの拡散によつ
て低減する方法。 (3) 酸化触媒や酸化剤あるいは吸着剤をフイルタ
ー部分又はシガレツトホルダー等に充填あるい
は保持してCOを酸化又は捕促して低減する方
法。 上記(1)〜(3)の方法の中、(1)、(2)の方法について
は現在までに広範な検討がなされており、その一
部については製品化もなされている。 しかし、(3)の方法については未だ決定的に有効
なものが見出されていないのが現状である。その
理由としては、たばこ煙と上記酸化触媒その他の
充填剤との接触時間が極めて短時間であること、
周囲環境に水分やタールなどの阻害成分が共存す
ること、充填剤自体の毒性を配慮する必要がある
ことのほかにたばこの香喫味が損なわれることな
ど多くの問題点が存することが挙げられる。 上記(3)の方法によりたばこ煙中のCOの低減す
る目的で提案された物質としては、例えば、酸化
銅と酸化マンガンの複合物を主体とした、いわゆ
るホプカリツト系複合酸化物触媒(特開昭51−
72988号、特開昭53−96399号)や、酸化マンガン
などの金属酸化物触媒(Brit.Pat.第1315374号)
があるが、いずれも水分による失活が著しく、追
試の結果では殆ど除去効果が認められない。又、
貴金属担持触媒についても多くの開示(特開昭55
−73344号、同53−149192号、同55−137039号)
があるが、追試した結果、煙中COの除去に関し
ては充分な効果を期待し得ないことが明らかとな
つた。 しかし、一方、エチレンを原料とし、気相中の
酸素を利用してアセトアルデヒドを合成する目的
で開発された、いわゆるワツカー(Wacker)型
の触媒は、COの酸化に対して高活性であり、
又、水を酸化還元(レドツクス)系内に有効に取
り込み、気相中の酸素によつてCOを酸化すると
いう機構が提案されている(ジヤーナル・エア・
ポリユーシヨン・コントロール・アソシエーシヨ
ン(J.Air Pollution Control Assoc.)28、253
(1978))。 このワツカー型触媒は、基本的には基質に対す
る活性化合物としてPdX2又はM2PdX2(Xはハロ
ゲン原子、Mは周期律表におけるa族金属)を
使用し、又、それに対するレドツクス対として
CuX2(Xはハロゲン原子)が用いられる。 一般に金属酸化物を用いた低温でのCOの酸化
において望ましくないとされる水分の存在が、こ
の系の触媒では逆に有効に働くため、たばこ煙中
のCO低減のように多湿な条件下での使用に際し
て格好の触媒ということができる。 このようなワツカー型触媒をCOの低減用に使
用した発明には、COによつて還元されたパルジ
ウム塩の再酸化を促進するために、ハロゲン化銅
以外の銅塩(主として硝酸銅)を第3成分として
添加して活性を高める方法(特開昭50−33990号
公報)や、同様に再酸化促進のためにスズイオン
等を添加する例(特開昭54−110400号公報)、1
価の銅塩を共存させた例(特開昭55−97252号公
報)がある。これらのCO酸化に関する発明にみ
られるワツカー型触媒は、溶液としての均一系、
あるいはアルミナ、シリカ、アルミノケイ酸塩、
モレキユラーシーブ、活性炭などの各種担体に担
持させた不均一系触媒として用いられている。 〔発明が解決しようとする問題点〕 しかし、かかる従来の発明によるワツカー型触
媒を触媒担体として公知である上述の担体に担持
させた触媒を、たばこ主流煙中のCOを低減する
目的で使用した場合には、その効果は必ずしも充
分でなく、一方、担体としてγ−アルミナを用い
た場合にはCOの酸化活性が高く、たばこのフイ
ルター部分に充填した場合のたばこ煙中のCO低
減率も極めて高いが、たばこ煙の香喫味を著しく
低下させるという欠点がある。これは、γ−アル
ミナ表面の物理、化学的性質によるものと考えら
れる。又、活性炭のみを担体とした場合には、た
ばこ香喫味へ及ぼす悪影響は認められなかつたも
のの、充分なCOの低減効果が得られないという
欠点がある。 本発明は従来のCO低減用触媒の上述した問題
点に鑑がみてなされたもので、たばこ煙中のCO
低減効果が高く、かつ、たばこ煙の香喫味に悪影
響を及ぼさないCO除去剤を提供することを目的
とする。 〔問題点を解決するための手段〕 CO除去剤を実際にたばこ、主としてシガレツ
トに適用するに際しては、CO除去剤を構成する
CO酸化触媒を担体に保持させてシガレツトのフ
イルターやホルダー内に充填して使用する必要が
ある。そこで、本発明者らは塩化パラジウムと塩
化第二銅の組合せからなるワツカー型触媒につい
て、これを担持すべき担体の種類とCOの酸化活
性との関係及びたばこ煙の香喫味に及ぼす影響等
について詳細に研究を行なつた結果、ベントナイ
トで固めた活性炭を担体とした場合に、高活性で
しかも香喫味に悪影響を及ぼさないCO除去触媒
が得られることを見出し本発明をなすに至つた。 すなわち、本発明は、ベントナイトと活性炭と
の混合組成物から成る担体に、塩化第二銅及び塩
化パラジウムの混合物を担持させたことを特徴と
するたばこ煙中の一酸化炭素除去剤である。 本発明において、担体の一組成物として使用さ
れる活性炭は特に制限はなく、ヤシガラ炭、パー
ム炭、針葉樹炭等の植物系活性炭もしくは石炭系
活性炭が好適に使用される。又、これらの活性炭
の比表面積はB.E.T.測定法による約500〜1300
m2/gを有するものであることが望ましい。 次に活性炭と混合使用されるベントナイトにつ
いても特に制限はないが、モンモリロナイト、ヘ
クトライトもしくは酸性白土等のいわゆる2:1
型の層状ケイ酸塩を主成分とした粘度鉱物の使用
が好ましい。 次に活性炭をベントナイトで固める方法として
は公知の方法でよく、例えば活性炭粉末とベント
ナイト粉末とをポリビニルアルコール等の水溶性
高分子水溶液で練り固め、10〜30メツシユ程度の
粒状に成型、予備乾燥したのち約100℃以上の温
度で加熱処理する等の方法が採用され得る。 この場合、活性炭とベントナイトの混合組成物
中に含有されるベントナイトの配合量は、活性炭
に対し10〜90重量%が好ましく、更に好ましくは
30〜70重量%が良い。 次に、本発明のCO除去剤中に含有される触媒
金属成分の担持量は、塩化パラジウムについては
0.01〜0.2mmol/gの範囲が良く、又、塩化第二
銅については0.1〜2.0mmol/g、好ましくは0.4
〜1.0mmol/gの範囲が良い。 上記の金属塩触媒をベントナイトで固めた活性
炭担体へ担持させる方法としては、予め担体の細
孔容積をB.E.T.法等で測定しておき、その容積
にほぼ等しい体積の水に塩化パラジウム及び塩化
第二銅を溶解し、この全量を担体の細孔内に吸収
させる、いわゆるポアフイリング法や、塩化パラ
ジウムと塩化第二銅の混合水溶液中に担体を浸漬
した後、ロータリーエバポレータ等を用いて溶液
を濃縮し担体上に塩類を析出させる、いわゆる含
浸法などの方法を適用することができるが、後者
の含浸法の方が簡便さの点、および活性成分の溶
液の濃度に特に制限を設ける必要がないことなど
から優れている。 以上のようにして調製された本発明のCO除去
剤はたばこのフイルター部分あるいはシガレツト
ホルダー等に充填して使用に供する。 〔発明の効果〕 以下実施例を掲げて本発明を更に詳しく説明す
るが、本発明のCO除去剤を使用すればたばこ煙
中のCOを顕著に低減することが可能となるのみ
ならず、たばこ煙の香喫味にも悪影響を与えず、
むしろ煙の刺激を軽減するなど優れた効果を有す
ることが判明した。 〔実施例〕 実施例 1 担体として、ヤシガラ活性炭とベントナイトの
10:7(重量比)混合組成物(以下単にヤシガラ
活性炭−ベントナイトと称する)、ヤシガラ活性
炭、γ−アルミナ、シリカおよびベントナイトを
それぞれ用い、これらの担体に塩化パラジウム担
持量を一定値0.07mmol/gとし、塩化第二銅の
比率を変えて担持させた場合の活性の差異を求め
た。 試験条件としては、まず、塩化パラジウム
0.1mol/および塩化第二銅0.1mol/の水溶液
をそれぞれ調製し、所定の担持量となるようにそ
れぞれの担体に前述の含浸法によつて含浸させ
た。 すなわち、担体それぞれ10gに対して前記塩化
パラジウム水溶液10mlをそれぞれ採取し、これに
前記塩化第二銅水溶液3ml、5ml、15mlおよび20
mlをそれぞれ加えた混液を調製した。次にそれぞ
れの混液にそれぞれの担体10gを別々に浸漬し、
水を減圧下で留去した後一夜風乾した。塩類の担
持量は原子吸光光度法で求めた。 又、活性の測定には、25℃において水蒸気で飽
和した標準ガス(CO:3%、O2:15%、He:82
%)を使用した。 試験は上記のようにしてそれぞれの担体に担持
させた触媒各100mgを内径6mmのガラス管に詰
め、上記標準ガスのパルス10mlを、毎分80mlの流
速に調節したヘリウムガスをキヤリヤーガスとし
て使用し触媒層を通過させた。触媒層通過後のガ
ス中のCO濃度を非分散型赤外分光光度計(ND−
IR)を使用して求めた。試験はすべて室温(25
℃)で行ない、一分間隔での3回のパルスによる
平均値からCO除去率を算出して求めた値を触媒
の担持量についてプロツトした結果は第1図に示
すとおりであつた。 第1図の結果から明らかなように、ヤシガラ活
性炭−ベントナイトを担体として使用した本発明
の触媒はγ−アルミナを担体とした触媒と同程度
で最高CO除去率90%以上の活性を示した。これ
に対し、ヤシガラ活性炭およびベントナイトをそ
れぞれ単独で用いた担体では、活性はいずれも30
%以下であり、活性炭とベントナイトとを混合し
た場合に相乗効果が発揮され、優れた担体が得ら
れることがわかる。さらに、塩化パラジウム担持
量を0.07mmol/gとしたときの最適な塩化第二
銅の担持量は、いずれの担体についても約0.5m
mol/gから0.7mmol/gの範囲であつた。 実施例 2 ヤシガラ活性炭−ベントナイトを担体とし、こ
れに塩化パラジウムと塩化第二銅の混合物を実施
例1と同様にして担持させた本発明の触媒につい
て、塩化パラジウムと塩化第二銅の担持量を夫々
変化させた場合のCO除去率を求めた結果は第2
図に示すとおりであつた。 なお、活性の測定法は触媒使用量を実施例1の
半量すなわち50mgとした以外は実施例1と同様の
条件で行なつた。 第2図の結果から、塩化パラジウム担持量が多
い程活性が向上することがわかる。又、塩化第二
銅の担持量は塩化パラジウム量が少なくなるにつ
れ、最適な担持量はやや少なくなる傾向がみられ
るが、CO除去率が最大となる担持量は約0.5m
mol/gと0.9mmol/gの間にあることがわか
る。 実施例 3 担体としての活性炭の種類を変えて調製した触
媒についてCO低減率を測定した結果を第1表に
示した。 なお、CO低減率の測定は実施例1と同様の条
件で実施した。
[Industrial Application Field] The present invention relates to a removing agent that selectively removes carbon monoxide from tobacco smoke generated during smoking without adversely affecting the flavor and aroma of tobacco. In general, carbon monoxide (hereinafter simply referred to as CO), which is generated by the incomplete combustion of carbon and carbon-containing compounds, binds tightly to hemoglobin in the blood.
Since it significantly inhibits the role of oxygen absorption and transport in the blood, it can cause acute poisoning symptoms such as headache and dizziness, and in severe cases can even lead to death. Also, CO
It is said that long-term exposure to can cause chronic heart disease. This CO is contained in a few percent of the so-called mainstream smoke that smokers directly inhale when they smoke cigarettes, and although it is significantly diluted by the air that is simultaneously inhaled before reaching the human lungs. It is believed that this contributes to the chronically elevated concentration of CO-binding hemoglobin in the blood of smokers, and reducing CO from tobacco smoke is an important issue that should be resolved immediately from the health perspective of smokers. has been done. [Prior Art] From this point of view, many attempts have been made to reduce the CO concentration in mainstream cigarette smoke.
Many proposals have been made in patent specifications and the like. These proposals can be broadly classified as follows. (1) A method of selecting and using raw materials that generate less CO. (2) A method of suppressing the generation of CO by creating holes in the filter or using high porosity wrapping paper, or reducing the generated CO by diffusion from the wrapping paper. (3) A method of reducing CO by oxidizing or capturing it by filling or retaining an oxidation catalyst, oxidizing agent, or adsorbent in a filter part or cigarette holder, etc. Among the methods (1) to (3) above, methods (1) and (2) have been extensively studied to date, and some of them have been commercialized. However, as for method (3), no definitively effective method has yet been found. The reason for this is that the contact time between tobacco smoke and the oxidation catalyst and other fillers is extremely short;
There are many problems such as the coexistence of inhibitory components such as moisture and tar in the surrounding environment, the need to take into account the toxicity of the filler itself, and the fact that the aroma and taste of the cigarette is impaired. Examples of substances that have been proposed for the purpose of reducing CO in tobacco smoke by the method (3) above include the so-called hopcalite-based composite oxide catalyst (Japanese Patent Application Laid-open No. 51−
No. 72988, JP-A-53-96399) and metal oxide catalysts such as manganese oxide (Brit.Pat. No. 1315374)
However, all of them are significantly deactivated by moisture, and follow-up tests show almost no removal effect. or,
There are also many disclosures regarding precious metal supported catalysts (Japanese Patent Application Laid-Open No. 1983-1999)
-73344, 53-149192, 55-137039)
However, as a result of further testing, it became clear that sufficient effectiveness could not be expected in removing CO from smoke. However, on the other hand, the so-called Wacker type catalyst, which was developed for the purpose of synthesizing acetaldehyde using ethylene as a raw material and using oxygen in the gas phase, has high activity against CO oxidation.
In addition, a mechanism has been proposed in which water is effectively incorporated into the redox system and CO is oxidized by oxygen in the gas phase (Journal Air
J. Air Pollution Control Assoc. 28, 253
(1978)). This Watzker type catalyst basically uses PdX 2 or M 2 PdX 2 (X is a halogen atom, M is a group A metal in the periodic table) as an active compound for the substrate, and also as a redox pair for the substrate.
CuX 2 (X is a halogen atom) is used. The presence of moisture, which is generally considered undesirable in low-temperature CO oxidation using metal oxides, works effectively in this type of catalyst, so it can be used under humid conditions such as when reducing CO in cigarette smoke. It can be said that it is an excellent catalyst for the use of Inventions using such Watzker-type catalysts for reducing CO include the addition of copper salts other than copper halides (mainly copper nitrate) to promote reoxidation of palladium salts reduced by CO. A method of increasing activity by adding three components (Japanese Patent Application Laid-open No. 50-33990), an example of adding tin ions, etc. to promote reoxidation (Japanese Patent Application Laid-open No. 110400/1983), 1
There is an example (Japanese Unexamined Patent Publication No. 55-97252) in which a copper salt of 20% is coexisting. The Watzker type catalyst seen in these inventions related to CO oxidation is a homogeneous system as a solution,
Or alumina, silica, aluminosilicate,
It is used as a heterogeneous catalyst supported on various carriers such as molecular sieves and activated carbon. [Problems to be Solved by the Invention] However, the catalyst in which the Watzker type catalyst according to the conventional invention is supported on the above-mentioned carrier, which is known as a catalyst carrier, was used for the purpose of reducing CO in mainstream cigarette smoke. On the other hand, when γ-alumina is used as a carrier, the oxidation activity of CO is high, and the rate of CO reduction in cigarette smoke when filled in the filter part of cigarettes is also extremely low. Although it is expensive, it has the disadvantage of significantly reducing the aroma and taste of tobacco smoke. This is considered to be due to the physical and chemical properties of the γ-alumina surface. Further, when activated carbon alone is used as a carrier, although no adverse effect on tobacco flavor was observed, there is a drawback that a sufficient CO reduction effect cannot be obtained. The present invention was made in view of the above-mentioned problems of conventional CO reduction catalysts, and it
The purpose of the present invention is to provide a CO removal agent that has a high reduction effect and does not adversely affect the aroma and taste of tobacco smoke. [Means for solving the problem] When actually applying a CO remover to cigarettes, mainly cigarettes, it is necessary to
It is necessary to hold the CO oxidation catalyst on a carrier and fill it in the filter or holder of a cigarette. Therefore, the present inventors investigated the relationship between the type of carrier on which the catalyst should be supported and the oxidation activity of CO, and the effect on the aroma and taste of tobacco smoke regarding the Watzker type catalyst consisting of a combination of palladium chloride and cupric chloride. As a result of detailed research, it was discovered that when activated carbon hardened with bentonite is used as a carrier, a highly active CO removal catalyst that does not adversely affect the aroma and taste can be obtained, leading to the present invention. That is, the present invention is a carbon monoxide remover in tobacco smoke, characterized in that a mixture of cupric chloride and palladium chloride is supported on a carrier made of a mixed composition of bentonite and activated carbon. In the present invention, the activated carbon used as a carrier composition is not particularly limited, and vegetable activated carbon or coal-based activated carbon such as coconut shell charcoal, palm charcoal, and softwood charcoal is preferably used. In addition, the specific surface area of these activated carbons is approximately 500 to 1300 according to the BET measurement method.
m 2 /g. Next, there are no particular restrictions on bentonite mixed with activated carbon, but there are so-called 2:1 bentonites such as montmorillonite, hectorite, or acid clay.
Preference is given to using clay minerals based on layered silicates of the type. Next, the activated carbon can be solidified with bentonite by any known method. For example, activated carbon powder and bentonite powder are kneaded with an aqueous solution of a water-soluble polymer such as polyvinyl alcohol, formed into particles of about 10 to 30 meshes, and pre-dried. A method such as heat treatment at a temperature of about 100° C. or higher may be adopted. In this case, the amount of bentonite contained in the mixed composition of activated carbon and bentonite is preferably 10 to 90% by weight, more preferably
30-70% by weight is good. Next, the supported amount of the catalytic metal component contained in the CO removal agent of the present invention is as follows for palladium chloride:
A good range is 0.01 to 0.2 mmol/g, and for cupric chloride, 0.1 to 2.0 mmol/g, preferably 0.4
The range of ~1.0 mmol/g is good. In order to support the above-mentioned metal salt catalyst on an activated carbon carrier hardened with bentonite, the pore volume of the carrier is measured in advance by the BET method, etc., and then palladium chloride and dichloromethane are added to a volume of water approximately equal to the pore volume of the carrier. The so-called pore-filling method involves dissolving copper and absorbing the entire amount into the pores of the carrier, or by immersing the carrier in a mixed aqueous solution of palladium chloride and cupric chloride, and then concentrating the solution using a rotary evaporator or the like. Methods such as the so-called impregnation method, in which salts are precipitated on the carrier, can be applied, but the latter impregnation method is simpler and does not require any particular restrictions on the concentration of the active ingredient solution. It is excellent because of The CO remover of the present invention prepared as described above is used by filling it into a cigarette filter or a cigarette holder. [Effects of the Invention] The present invention will be explained in more detail with reference to Examples below. By using the CO remover of the present invention, it is possible not only to significantly reduce CO in tobacco smoke, but also to reduce the amount of CO contained in tobacco smoke. It does not have a negative effect on the aroma and taste of smoke,
In fact, it was found to have excellent effects such as reducing the irritation caused by smoke. [Example] Example 1 Using coconut shell activated carbon and bentonite as carriers
A 10:7 (weight ratio) mixed composition (hereinafter simply referred to as coconut shell activated carbon-bentonite), coconut shell activated carbon, γ-alumina, silica, and bentonite were used, and the amount of palladium chloride supported on these supports was set at a constant value of 0.07 mmol/g. The difference in activity was determined when different ratios of cupric chloride were supported. As for the test conditions, first, palladium chloride
Aqueous solutions of 0.1 mol/copper chloride and 0.1 mol/copper chloride were respectively prepared, and each carrier was impregnated with the above-mentioned impregnation method so as to have a predetermined supported amount. That is, 10 ml of the above palladium chloride aqueous solution was collected for each 10 g of the carrier, and 3 ml, 5 ml, 15 ml and 20 ml of the cupric chloride aqueous solution were collected.
A mixed solution was prepared by adding ml of each. Next, 10 g of each carrier was separately immersed in each mixed solution,
After water was distilled off under reduced pressure, the mixture was air-dried overnight. The amount of supported salts was determined by atomic absorption spectrometry. In addition, to measure the activity, standard gases saturated with water vapor (CO: 3%, O 2 : 15%, He: 82
%)It was used. In the test, 100 mg of each catalyst supported on each carrier as described above was packed into a glass tube with an inner diameter of 6 mm, and pulsed 10 ml of the above standard gas was applied to the catalyst using helium gas adjusted to a flow rate of 80 ml per minute as a carrier gas. passed through the layers. The CO concentration in the gas after passing through the catalyst layer was measured using a non-dispersive infrared spectrophotometer (ND-
IR). All tests were performed at room temperature (25
The CO removal rate was calculated from the average value of three pulses at one-minute intervals, and the value was plotted against the amount of catalyst supported, and the results were as shown in Figure 1. As is clear from the results shown in FIG. 1, the catalyst of the present invention using coconut shell activated carbon-bentonite as a carrier exhibited a maximum CO removal rate of 90% or more, which was comparable to the catalyst using γ-alumina as a carrier. On the other hand, when coconut shell activated carbon and bentonite were used alone, the activity was 30.
% or less, and it can be seen that when activated carbon and bentonite are mixed, a synergistic effect is exhibited and an excellent carrier can be obtained. Furthermore, when the amount of palladium chloride supported is 0.07 mmol/g, the optimal amount of cupric chloride supported is approximately 0.5 mmol/g for any carrier.
It ranged from mol/g to 0.7 mmol/g. Example 2 Regarding the catalyst of the present invention in which coconut shell activated carbon-bentonite was used as a carrier and a mixture of palladium chloride and cupric chloride was supported on it in the same manner as in Example 1, the amount of supported palladium chloride and cupric chloride was determined. The results of calculating the CO removal rate when each change is shown in the second section.
It was as shown in the figure. The activity was measured under the same conditions as in Example 1, except that the amount of catalyst used was half that of Example 1, ie, 50 mg. From the results shown in FIG. 2, it can be seen that the activity improves as the amount of palladium chloride supported increases. In addition, the optimum amount of cupric chloride supported tends to decrease slightly as the amount of palladium chloride decreases, but the supported amount at which the CO removal rate is maximum is approximately 0.5 m
It can be seen that it is between mol/g and 0.9 mmol/g. Example 3 Table 1 shows the results of measuring CO reduction rates for catalysts prepared by changing the type of activated carbon used as a carrier. Note that the CO reduction rate was measured under the same conditions as in Example 1.

【表】 第1表の結果から、いずれの試料においてもベ
ントナイトを用いて固めた活性炭を担体とした本
発明の触媒は、活性炭のみを担体とした触媒に比
し、活性炭の種類に関係なく著しく高いCO低減
率を示すことがわかる。 実施例 4 第1表に示した試料触媒のうち、1−1、1−
2および1−3の担体および触媒をそれぞれ200
gはかりとり、これを内径5mm、長さ25mmのガラ
ス管に充填し、ガラス管の両端をガラスウールで
押えた。 このガラス管の一端を製品シガレツト(商品名
ハイライト)のフイルター部分にセロハンテープ
を用いて接続した。又、このガラス管の他端を自
動喫煙装置に接続し、標準喫煙条件(35ml吸引/
1パフ、2秒/1パフ、1パフ/分、すいがら長
30mm)で吸煙させ、得られた主流煙ガス中のCO
濃度をND−IRを用いて測定した結果、1−3の
本発明の試料を充填したガラス管を取付けたシガ
レツトでは1−1、1−2の試料に比しそれぞれ
28%及び20%減少した。 実施例 5 実施例3の第1表に示される試料のうち、2−
1及び2−2の触媒各400mgをはかりとり、内径
6mm、長さ50mmのガラス管に充填し、ガラス管の
両端をグラスウールで押えた。このガラス管の一
端にゴム製の吸い口を取付け、シガレツト(商品
名ハイライト)のフイルター部を挿入した。この
ガラス管の他端を自動喫煙装置に取付け、前記と
同様の標準喫煙条件で吸煙させた。一本のシガレ
ツトの吸煙終了後、主流煙ガス中のCO濃度をND
−IRで測定した。測定終了後2本目のシガレツ
トを取付け、同様に吸煙、測定を繰り返し、一つ
のガラス管につき合計10本のシガレツトの吸煙を
行なわせた。又、別に第1表の試料2−2と同一
の担体を用いたもので塩化パラジウムと塩化第二
銅を担持させないものをコントロールとした。 この結果、1本目のシガレツトについてみる
と、本発明の2−2の試料を通過した主流煙中の
COは2−1の試料に比し24%、コントロールに
比し52%の減少がみられた。又、2本目では2−
1の試料に比し26%、コントロールに比し40%
と、それぞれ減少しており、10本目においても2
−2の試料では2−1の試料に比し14%、コント
ロールに比し26%の減少が夫々認められた。 実施例 6 γ−アルミナを担体として、これに塩化パラジ
ウム0.07mmol/g、塩化第二銅0.7mmol/gの
比率で触媒を担持させたγ−アルミナ担持触媒
と、ヤシガラ活性炭−ベントナイト担体に塩化パ
ラジウムと塩化第二銅とを同様の比率で担持させ
た本発明のヤシガラ活性炭−ベントナイト担体触
媒とを夫々200mgを製品シガレツト(商品名ハイ
ライト)のフイルター部分にトリプルフイルター
型式で充填した。一方、触媒無担持のヤシガラ炭
200mgを同様にフイルター部分に充填したシガレ
ツトを対照品として、訓練された専門官能検査パ
ネル10名によるたばこ煙の香喫味評価を行なつた
結果を第2表に示した。
[Table] From the results in Table 1, it can be seen that in all samples, the catalyst of the present invention using bentonite-hardened activated carbon as a carrier was significantly more effective than the catalyst using only activated carbon as a carrier, regardless of the type of activated carbon. It can be seen that this shows a high CO reduction rate. Example 4 Among the sample catalysts shown in Table 1, 1-1, 1-
2 and 1-3 supports and catalysts at 200% each
A glass tube with an inner diameter of 5 mm and a length of 25 mm was filled with the sample, and both ends of the glass tube were pressed with glass wool. One end of this glass tube was connected to the filter part of a product cigarette (trade name Highlight) using cellophane tape. Also, connect the other end of this glass tube to an automatic smoking device and set it under standard smoking conditions (35ml suction/
1 puff, 2 seconds/1 puff, 1 puff/minute, watermelon length
30mm), CO in the obtained mainstream smoke gas
As a result of measuring the concentration using ND-IR, the cigarettes equipped with the glass tube filled with the sample of the present invention of 1-3 had a lower concentration than the samples of 1-1 and 1-2, respectively.
decreased by 28% and 20%. Example 5 Among the samples shown in Table 1 of Example 3, 2-
400 mg each of catalysts 1 and 2-2 were weighed out and filled into a glass tube with an inner diameter of 6 mm and a length of 50 mm, and both ends of the glass tube were pressed with glass wool. A rubber mouthpiece was attached to one end of the glass tube, and the filter part of a cigarette (trade name: Highlight) was inserted. The other end of this glass tube was attached to an automatic smoking device and smoked under the same standard smoking conditions as above. After smoking a single cigarette, the CO concentration in the mainstream smoke gas is determined by ND.
- Measured by IR. After the measurement was completed, a second cigarette was attached, and smoking and measurement were repeated in the same manner, with a total of 10 cigarettes being smoked from each glass tube. Separately, a sample using the same carrier as Sample 2-2 in Table 1 but without supporting palladium chloride and cupric chloride was used as a control. As a result, when looking at the first cigarette, it was found that the mainstream smoke that passed through the sample 2-2 of the present invention
CO was reduced by 24% compared to the 2-1 sample and 52% compared to the control. Also, in the second one, 2-
26% compared to sample 1, 40% compared to control
, and decreased by 2 even in the 10th test.
The -2 sample showed a 14% decrease compared to the 2-1 sample, and a 26% decrease compared to the control. Example 6 A γ-alumina supported catalyst in which a catalyst was supported on γ-alumina at a ratio of 0.07 mmol/g of palladium chloride and 0.7 mmol/g of cupric chloride, and palladium chloride on a coconut shell activated carbon-bentonite carrier. 200 mg of each of the coconut shell activated carbon-bentonite carrier catalyst of the present invention, which supported the same proportions of cupric chloride and cupric chloride, was packed into the filter portion of a product cigarette (trade name Highlight) in a triple filter format. On the other hand, coconut husk charcoal without catalyst support
Table 2 shows the results of an evaluation of the aroma and taste of tobacco smoke by a trained expert panel of 10 people, using a cigarette similarly filled with 200 mg in the filter part as a control product.

【表】 第2表の評価にみられるように、本発明のヤシ
ガラ活性炭−ベントナイト担体触媒はたばこ煙の
香喫味に与える悪影響はほとんどなく、パネル全
員が対照品と差がなく香喫味が優れていると評価
した。一方、γ−アルミナ担持触媒はたばこの香
喫味に著しく負の影響を与えることがわかる。 以上、実施例を含めて詳細に説明したように、
活性炭−ベントナイト担体に塩化パラジウムと塩
化第二銅とからなる触媒を担持させて成る本発明
のCO除去剤は、たばこ煙の香喫味を低下させる
ことなく、煙中のCOを顕著に低減させることが
でき、喫煙者の健康管理上極めて有益な発明であ
る。
[Table] As seen in the evaluation in Table 2, the coconut shell activated carbon-bentonite carrier catalyst of the present invention has almost no adverse effect on the flavor of tobacco smoke, and all the panelists said that it had an excellent flavor and flavor with no difference from the control product. It was evaluated that there is. On the other hand, it can be seen that the γ-alumina supported catalyst has a significant negative influence on the aroma and taste of cigarettes. As explained above in detail including the examples,
The CO remover of the present invention, which comprises a catalyst made of palladium chloride and cupric chloride supported on an activated carbon-bentonite carrier, can significantly reduce CO in smoke without reducing the aroma and taste of tobacco smoke. This invention is extremely useful for the health management of smokers.

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

第1図は各種担体を使用し、塩化パラジウムに
対する塩化第二銅の比率を変化させた場合のCO
除去率を示すグラフ、第2図はヤシガラ活性炭−
ベントナイトを担体として使用し、塩化パラジウ
ムと塩化第二銅の担持量を変化させた場合のCO
除去率を示すグラフである。
Figure 1 shows the CO2 emissions when various carriers are used and the ratio of cupric chloride to palladium chloride is varied.
A graph showing the removal rate, Figure 2 is coconut shell activated carbon.
CO when using bentonite as a carrier and varying the supported amounts of palladium chloride and cupric chloride
It is a graph showing a removal rate.

Claims (1)

【特許請求の範囲】[Claims] 1 ベントナイトと活性炭との混合組成物から成
る担体に、塩化第二銅及び塩化パラジウムの混合
物を担持させたことを特徴とするたばこ煙中の一
酸化炭素除去剤。
1. A carbon monoxide remover in tobacco smoke, characterized in that a mixture of cupric chloride and palladium chloride is supported on a carrier made of a mixed composition of bentonite and activated carbon.
JP8020084A 1984-04-23 1984-04-23 Agent for removing carbon monooxide in tobacco smoke Granted JPS60224483A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8020084A JPS60224483A (en) 1984-04-23 1984-04-23 Agent for removing carbon monooxide in tobacco smoke

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8020084A JPS60224483A (en) 1984-04-23 1984-04-23 Agent for removing carbon monooxide in tobacco smoke

Publications (2)

Publication Number Publication Date
JPS60224483A JPS60224483A (en) 1985-11-08
JPS6211582B2 true JPS6211582B2 (en) 1987-03-13

Family

ID=13711741

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8020084A Granted JPS60224483A (en) 1984-04-23 1984-04-23 Agent for removing carbon monooxide in tobacco smoke

Country Status (1)

Country Link
JP (1) JPS60224483A (en)

Also Published As

Publication number Publication date
JPS60224483A (en) 1985-11-08

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