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JPS6211582B2 - - Google Patents
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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

【発明の詳现な説明】[Detailed description of the invention]

〔産業䞊の利甚分野〕 本発明は、たばこの銙喫味に悪圱響を及がすこ
ずなく喫煙時に発生するたばこ煙から䞀酞化炭玠
を遞択的に陀去する陀去剀に関する。 䞀般に、炭玠や含炭玠化合物の䞍完党燃焌によ
぀お発生する䞀酞化炭玠以䞋単にCOずもい
うは、血液䞭のヘモグロビンず匷固に結合し、
血液の酞玠吞収及び運搬の圹割を著しく阻害する
ため、頭痛、めたいなどの急性䞭毒症状をひき起
し、甚だしい堎合には死に至らしめる。又、CO
に長期的に暎露された堎合には慢性心臓疟患を喚
起するずいわれおいる。 このCOは喫煙者がたばこを喫煙した際に盎接
吞入する煙いわゆる䞻流煙䞭にも数パヌセント含
有されおおり、これは人䜓の肺に達するたでに同
時に吞入される空気により倧幅に垌釈されるもの
の、喫煙者の血䞭CO結合ヘモグロビンの慢性的
な濃床䞊昇に寄䞎しおいるずされ、たばこ煙䞭か
らのCOの䜎枛は喫煙者の健康䞊の芳点から早急
に解決をはかるべき重芁な課題ずされおいる。 〔埓来の技術〕 埓来、かかる芳点からたばこ䞻流煙䞭のCO濃
床を䜎枛させようずする詊みが盛んに行なわれ、
特蚱明现曞等においお倚くの提案がなされおい
る。 これらの提案は倧別するず以䞋のように分類す
るこずができる。 (1) COの生成の少ない原料を遞択しお䜿甚する
方法。 (2) フむルタヌ郚分に開孔を蚭け、あるいは巻玙
に高気孔床のものを䜿甚しおCOの生成を抑制
したり、生成したCOを巻玙からの拡散によ぀
お䜎枛する方法。 (3) 酞化觊媒や酞化剀あるいは吞着剀をフむルタ
ヌ郚分又はシガレツトホルダヌ等に充填あるい
は保持しおCOを酞化又は捕促しお䜎枛する方
法。 䞊蚘(1)〜(3)の方法の䞭、(1)、(2)の方法に぀いお
は珟圚たでに広範な怜蚎がなされおおり、その䞀
郚に぀いおは補品化もなされおいる。 しかし、(3)の方法に぀いおは未だ決定的に有効
なものが芋出されおいないのが珟状である。その
理由ずしおは、たばこ煙ず䞊蚘酞化觊媒その他の
充填剀ずの接觊時間が極めお短時間であるこず、
呚囲環境に氎分やタヌルなどの阻害成分が共存す
るこず、充填剀自䜓の毒性を配慮する必芁がある
こずのほかにたばこの銙喫味が損なわれるこずな
ど倚くの問題点が存するこずが挙げられる。 䞊蚘(3)の方法によりたばこ煙䞭のCOの䜎枛す
る目的で提案された物質ずしおは、䟋えば、酞化
銅ず酞化マンガンの耇合物を䞻䜓ずした、いわゆ
るホプカリツト系耇合酞化物觊媒特開昭51−
72988号、特開昭53−96399号や、酞化マンガン
などの金属酞化物觊媒Brit.Pat.第1315374号
があるが、いずれも氎分による倱掻が著しく、远
詊の結果では殆ど陀去効果が認められない。又、
貎金属担持觊媒に぀いおも倚くの開瀺特開昭55
−73344号、同53−149192号、同55−137039号
があるが、远詊した結果、煙䞭COの陀去に関し
おは充分な効果を期埅し埗ないこずが明らかずな
぀た。 しかし、䞀方、゚チレンを原料ずし、気盞䞭の
酞玠を利甚しおアセトアルデヒドを合成する目的
で開発された、いわゆるワツカヌWacker型
の觊媒は、COの酞化に察しお高掻性であり、
又、氎を酞化還元レドツクス系内に有効に取
り蟌み、気盞䞭の酞玠によ぀おCOを酞化するず
いう機構が提案されおいるゞダヌナル・゚ア・
ポリナヌシペン・コントロヌル・ア゜シ゚ヌシペ
ンJ.Air Pollution Control Assoc.28、253
1978。 このワツカヌ型觊媒は、基本的には基質に察す
る掻性化合物ずしおPdX2又はM2PdX2はハロ
ゲン原子、は呚期埋衚における族金属を
䜿甚し、又、それに察するレドツクス察ずしお
CuX2はハロゲン原子が甚いられる。 䞀般に金属酞化物を甚いた䜎枩でのCOの酞化
においお望たしくないずされる氎分の存圚が、こ
の系の觊媒では逆に有効に働くため、たばこ煙䞭
のCO䜎枛のように倚湿な条件䞋での䜿甚に際し
お栌奜の觊媒ずいうこずができる。 このようなワツカヌ型觊媒をCOの䜎枛甚に䜿
甚した発明には、COによ぀お還元されたパルゞ
りム塩の再酞化を促進するために、ハロゲン化銅
以倖の銅塩䞻ずしお硝酞銅を第成分ずしお
添加しお掻性を高める方法特開昭50−33990号
公報や、同様に再酞化促進のためにスズむオン
等を添加する䟋特開昭54−110400号公報、
䟡の銅塩を共存させた䟋特開昭55−97252号公
報がある。これらのCO酞化に関する発明にみ
られるワツカヌ型觊媒は、溶液ずしおの均䞀系、
あるいはアルミナ、シリカ、アルミノケむ酞塩、
モレキナラヌシヌブ、掻性炭などの各皮担䜓に担
持させた䞍均䞀系觊媒ずしお甚いられおいる。 〔発明が解決しようずする問題点〕 しかし、かかる埓来の発明によるワツカヌ型觊
媒を觊媒担䜓ずしお公知である䞊述の担䜓に担持
させた觊媒を、たばこ䞻流煙䞭のCOを䜎枛する
目的で䜿甚した堎合には、その効果は必ずしも充
分でなく、䞀方、担䜓ずしおγ−アルミナを甚い
た堎合にはCOの酞化掻性が高く、たばこのフむ
ルタヌ郚分に充填した堎合のたばこ煙䞭のCO䜎
枛率も極めお高いが、たばこ煙の銙喫味を著しく
䜎䞋させるずいう欠点がある。これは、γ−アル
ミナ衚面の物理、化孊的性質によるものず考えら
れる。又、掻性炭のみを担䜓ずした堎合には、た
ばこ銙喫味ぞ及がす悪圱響は認められなか぀たも
のの、充分なCOの䜎枛効果が埗られないずいう
欠点がある。 本発明は埓来のCO䜎枛甚觊媒の䞊述した問題
点に鑑がみおなされたもので、たばこ煙䞭のCO
䜎枛効果が高く、か぀、たばこ煙の銙喫味に悪圱
響を及がさないCO陀去剀を提䟛するこずを目的
ずする。 〔問題点を解決するための手段〕 CO陀去剀を実際にたばこ、䞻ずしおシガレツ
トに適甚するに際しおは、CO陀去剀を構成する
CO酞化觊媒を担䜓に保持させおシガレツトのフ
むルタヌやホルダヌ内に充填しお䜿甚する必芁が
ある。そこで、本発明者らは塩化パラゞりムず塩
化第二銅の組合せからなるワツカヌ型觊媒に぀い
お、これを担持すべき担䜓の皮類ずCOの酞化掻
性ずの関係及びたばこ煙の銙喫味に及がす圱響等
に぀いお詳现に研究を行な぀た結果、ベントナむ
トで固めた掻性炭を担䜓ずした堎合に、高掻性で
しかも銙喫味に悪圱響を及がさないCO陀去觊媒
が埗られるこずを芋出し本発明をなすに至぀た。 すなわち、本発明は、ベントナむトず掻性炭ず
の混合組成物から成る担䜓に、塩化第二銅及び塩
化パラゞりムの混合物を担持させたこずを特城ず
するたばこ煙䞭の䞀酞化炭玠陀去剀である。 本発明においお、担䜓の䞀組成物ずしお䜿甚さ
れる掻性炭は特に制限はなく、ダシガラ炭、パヌ
ム炭、針葉暹炭等の怍物系掻性炭もしくは石炭系
掻性炭が奜適に䜿甚される。又、これらの掻性炭
の比衚面積はB.E.T.枬定法による玄500〜1300
m2を有するものであるこずが望たしい。 次に掻性炭ず混合䜿甚されるベントナむトに぀
いおも特に制限はないが、モンモリロナむト、ヘ
クトラむトもしくは酞性癜土等のいわゆる
型の局状ケむ酞塩を䞻成分ずした粘床鉱物の䜿甚
が奜たしい。 次に掻性炭をベントナむトで固める方法ずしお
は公知の方法でよく、䟋えば掻性炭粉末ずベント
ナむト粉末ずをポリビニルアルコヌル等の氎溶性
高分子氎溶液で緎り固め、10〜30メツシナ皋床の
粒状に成型、予備也燥したのち玄100℃以䞊の枩
床で加熱凊理する等の方法が採甚され埗る。 この堎合、掻性炭ずベントナむトの混合組成物
䞭に含有されるベントナむトの配合量は、掻性炭
に察し10〜90重量が奜たしく、曎に奜たしくは
30〜70重量が良い。 次に、本発明のCO陀去剀䞭に含有される觊媒
金属成分の担持量は、塩化パラゞりムに぀いおは
0.01〜0.2molの範囲が良く、又、塩化第二
銅に぀いおは0.1〜2.0mol、奜たしくは0.4
〜1.0molの範囲が良い。 䞊蚘の金属塩觊媒をベントナむトで固めた掻性
炭担䜓ぞ担持させる方法ずしおは、予め担䜓の现
孔容積をB.E.T.法等で枬定しおおき、その容積
にほが等しい䜓積の氎に塩化パラゞりム及び塩化
第二銅を溶解し、この党量を担䜓の现孔内に吞収
させる、いわゆるポアフむリング法や、塩化パラ
ゞりムず塩化第二銅の混合氎溶液䞭に担䜓を浞挬
した埌、ロヌタリヌ゚バポレヌタ等を甚いお溶液
を濃瞮し担䜓䞊に塩類を析出させる、いわゆる含
浞法などの方法を適甚するこずができるが、埌者
の含浞法の方が簡䟿さの点、および掻性成分の溶
液の濃床に特に制限を蚭ける必芁がないこずなど
から優れおいる。 以䞊のようにしお調補された本発明のCO陀去
剀はたばこのフむルタヌ郚分あるいはシガレツト
ホルダヌ等に充填しお䜿甚に䟛する。 〔発明の効果〕 以䞋実斜䟋を掲げお本発明を曎に詳しく説明す
るが、本発明のCO陀去剀を䜿甚すればたばこ煙
䞭のCOを顕著に䜎枛するこずが可胜ずなるのみ
ならず、たばこ煙の銙喫味にも悪圱響を䞎えず、
むしろ煙の刺激を軜枛するなど優れた効果を有す
るこずが刀明した。 〔実斜䟋〕 実斜䟋  担䜓ずしお、ダシガラ掻性炭ずベントナむトの
10重量比混合組成物以䞋単にダシガラ
掻性炭−ベントナむトず称する、ダシガラ掻性
炭、γ−アルミナ、シリカおよびベントナむトを
それぞれ甚い、これらの担䜓に塩化パラゞりム担
持量を䞀定倀0.07molずし、塩化第二銅の
比率を倉えお担持させた堎合の掻性の差異を求め
た。 詊隓条件ずしおは、たず、塩化パラゞりム
0.1molおよび塩化第二銅0.1molの氎溶液
をそれぞれ調補し、所定の担持量ずなるようにそ
れぞれの担䜓に前述の含浞法によ぀お含浞させ
た。 すなわち、担䜓それぞれ10に察しお前蚘塩化
パラゞりム氎溶液10mlをそれぞれ採取し、これに
前蚘塩化第二銅氎溶液ml、ml、15mlおよび20
mlをそれぞれ加えた混液を調補した。次にそれぞ
れの混液にそれぞれの担䜓10を別々に浞挬し、
氎を枛圧䞋で留去した埌䞀倜颚也した。塩類の担
持量は原子吞光光床法で求めた。 又、掻性の枬定には、25℃においお氎蒞気で飜
和した暙準ガスCO、O215、He82
を䜿甚した。 詊隓は䞊蚘のようにしおそれぞれの担䜓に担持
させた觊媒各100mgを内埄mmのガラス管に詰
め、䞊蚘暙準ガスのパルス10mlを、毎分80mlの流
速に調節したヘリりムガスをキダリダヌガスずし
お䜿甚し觊媒局を通過させた。觊媒局通過埌のガ
ス䞭のCO濃床を非分散型赀倖分光光床蚈ND−
IRを䜿甚しお求めた。詊隓はすべお宀枩25
℃で行ない、䞀分間隔での回のパルスによる
平均倀からCO陀去率を算出しお求めた倀を觊媒
の担持量に぀いおプロツトした結果は第図に瀺
すずおりであ぀た。 第図の結果から明らかなように、ダシガラ掻
性炭−ベントナむトを担䜓ずしお䜿甚した本発明
の觊媒はγ−アルミナを担䜓ずした觊媒ず同皋床
で最高CO陀去率90以䞊の掻性を瀺した。これ
に察し、ダシガラ掻性炭およびベントナむトをそ
れぞれ単独で甚いた担䜓では、掻性はいずれも30
以䞋であり、掻性炭ずベントナむトずを混合し
た堎合に盞乗効果が発揮され、優れた担䜓が埗ら
れるこずがわかる。さらに、塩化パラゞりム担持
量を0.07molずしたずきの最適な塩化第二
銅の担持量は、いずれの担䜓に぀いおも玄0.5
molから0.7molの範囲であ぀た。 実斜䟋  ダシガラ掻性炭−ベントナむトを担䜓ずし、こ
れに塩化パラゞりムず塩化第二銅の混合物を実斜
䟋ず同様にしお担持させた本発明の觊媒に぀い
お、塩化パラゞりムず塩化第二銅の担持量を倫々
倉化させた堎合のCO陀去率を求めた結果は第
図に瀺すずおりであ぀た。 なお、掻性の枬定法は觊媒䜿甚量を実斜䟋の
半量すなわち50mgずした以倖は実斜䟋ず同様の
条件で行な぀た。 第図の結果から、塩化パラゞりム担持量が倚
い皋掻性が向䞊するこずがわかる。又、塩化第二
銅の担持量は塩化パラゞりム量が少なくなるに぀
れ、最適な担持量はやや少なくなる傟向がみられ
るが、CO陀去率が最倧ずなる担持量は玄0.5
molず0.9molの間にあるこずがわか
る。 実斜䟋  担䜓ずしおの掻性炭の皮類を倉えお調補した觊
媒に぀いおCO䜎枛率を枬定した結果を第衚に
瀺した。 なお、CO䜎枛率の枬定は実斜䟋ず同様の条
件で実斜した。
[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.

【衚】 第衚の結果から、いずれの詊料においおもベ
ントナむトを甚いお固めた掻性炭を担䜓ずした本
発明の觊媒は、掻性炭のみを担䜓ずした觊媒に比
し、掻性炭の皮類に関係なく著しく高いCO䜎枛
率を瀺すこずがわかる。 実斜䟋  第衚に瀺した詊料觊媒のうち、−、−
および−の担䜓および觊媒をそれぞれ200
はかりずり、これを内埄mm、長さ25mmのガラ
ス管に充填し、ガラス管の䞡端をガラスりヌルで
抌えた。 このガラス管の䞀端を補品シガレツト商品名
ハむラむトのフむルタヌ郚分にセロハンテヌプ
を甚いお接続した。又、このガラス管の他端を自
動喫煙装眮に接続し、暙準喫煙条件35ml吞匕
パフ、秒パフ、パフ分、すいがら長
30mmで吞煙させ、埗られた䞻流煙ガス䞭のCO
濃床をND−IRを甚いお枬定した結果、−の
本発明の詊料を充填したガラス管を取付けたシガ
レツトでは−、−の詊料に比しそれぞれ
28及び20枛少した。 実斜䟋  実斜䟋の第衚に瀺される詊料のうち、−
及び−の觊媒各400mgをはかりずり、内埄
mm、長さ50mmのガラス管に充填し、ガラス管の
䞡端をグラスりヌルで抌えた。このガラス管の䞀
端にゎム補の吞い口を取付け、シガレツト商品
名ハむラむトのフむルタヌ郚を挿入した。この
ガラス管の他端を自動喫煙装眮に取付け、前蚘ず
同様の暙準喫煙条件で吞煙させた。䞀本のシガレ
ツトの吞煙終了埌、䞻流煙ガス䞭のCO濃床をND
−IRで枬定した。枬定終了埌本目のシガレツ
トを取付け、同様に吞煙、枬定を繰り返し、䞀぀
のガラス管に぀き合蚈10本のシガレツトの吞煙を
行なわせた。又、別に第衚の詊料−ず同䞀
の担䜓を甚いたもので塩化パラゞりムず塩化第二
銅を担持させないものをコントロヌルずした。 この結果、本目のシガレツトに぀いおみる
ず、本発明の−の詊料を通過した䞻流煙䞭の
COは−の詊料に比し24、コントロヌルに
比し52の枛少がみられた。又、本目では−
の詊料に比し26、コントロヌルに比し40
ず、それぞれ枛少しおおり、10本目においおも
−の詊料では−の詊料に比し14、コント
ロヌルに比し26の枛少が倫々認められた。 実斜䟋  γ−アルミナを担䜓ずしお、これに塩化パラゞ
りム0.07mol、塩化第二銅0.7molの
比率で觊媒を担持させたγ−アルミナ担持觊媒
ず、ダシガラ掻性炭−ベントナむト担䜓に塩化パ
ラゞりムず塩化第二銅ずを同様の比率で担持させ
た本発明のダシガラ掻性炭−ベントナむト担䜓觊
媒ずを倫々200mgを補品シガレツト商品名ハむ
ラむトのフむルタヌ郚分にトリプルフむルタヌ
型匏で充填した。䞀方、觊媒無担持のダシガラ炭
200mgを同様にフむルタヌ郚分に充填したシガレ
ツトを察照品ずしお、蚓緎された専門官胜怜査パ
ネル10名によるたばこ煙の銙喫味評䟡を行な぀た
結果を第衚に瀺した。
[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.

【衚】 第衚の評䟡にみられるように、本発明のダシ
ガラ掻性炭−ベントナむト担䜓觊媒はたばこ煙の
銙喫味に䞎える悪圱響はほずんどなく、パネル党
員が察照品ず差がなく銙喫味が優れおいるず評䟡
した。䞀方、γ−アルミナ担持觊媒はたばこの銙
喫味に著しく負の圱響を䞎えるこずがわかる。 以䞊、実斜䟋を含めお詳现に説明したように、
掻性炭−ベントナむト担䜓に塩化パラゞりムず塩
化第二銅ずからなる觊媒を担持させお成る本発明
のCO陀去剀は、たばこ煙の銙喫味を䜎䞋させる
こずなく、煙䞭のCOを顕著に䜎枛させるこずが
でき、喫煙者の健康管理䞊極めお有益な発明であ
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図は各皮担䜓を䜿甚し、塩化パラゞりムに
察する塩化第二銅の比率を倉化させた堎合のCO
陀去率を瀺すグラフ、第図はダシガラ掻性炭−
ベントナむトを担䜓ずしお䜿甚し、塩化パラゞり
ムず塩化第二銅の担持量を倉化させた堎合のCO
陀去率を瀺すグラフである。
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)

【特蚱請求の範囲】[Claims]  ベントナむトず掻性炭ずの混合組成物から成
る担䜓に、塩化第二銅及び塩化パラゞりムの混合
物を担持させたこずを特城ずするたばこ煙䞭の䞀
酞化炭玠陀去剀。
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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